[ChemSep]
Version=6.01
Name=Z:\big\cs\databases\howto_distillation\howto_distillation.sep
Title=Montz B1-250

[Paths]
Device drivers path=c:\temp\cs\windows\wincs\
Help and Info path=c:\temp\cs\__cs\help\
Component data path=c:\temp\cs\__cs\pcd\
Property data path=c:\temp\cs\__cs\ipd\
Section data path=c:\temp\cs\__cs\ild\
Executables path=c:\temp\cs\exes
Temporary path=WINTMPDIR
Scripts path=c:\temp\cs\windows\wincs\

[Units]
Temperature=øC
Flow=mol/s
Mass flow=kg/s
Pressure=kPa
Heat=W
Enthalpy=J/kmol
Entropy=J/kmol/K
Fraction=Ä
Length=m
1/Length=1/m
Area=mý
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/m2/K
Diffusivity=mý/s
Interaction parameter=J/mol
Time=s

[Components]
2
151 505 Library Offset, Index, CAS=95-47-6 CID=O-xylene
Name=O-xylene
Lib=c:\temp\cs\__cs\pcd\chemsep1.pcd
152 507 Library Offset, Index, CAS=106-42-3 CID=P-xylene
Name=P-xylene
Lib=c:\temp\cs\__cs\pcd\chemsep1.pcd

[Operation]
3 Operation NonEquilibrium Column
12 Operation kind Total Reflux Column
2 Condenser Total (Subcooled product)
2 Reboiler Total (Vapour product)
66 Stages
1 Feed stages
0 Sidestream stages
F=65
S=
0 Pumparound stages
P=

[Properties]

[Thermodynamics]
3 K model Gamma-Phi
1 Activity coefficient Ideal solution
*  Wilson model *
*  UNIQUAC model *
1 Equation of State Ideal gas law
*  Cubic EOS *
*  Virial EOS *
1 Vapour pressure Antoine

[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
2 First stage
65 Last stage

[Sections]
1 System factor
1 Number
3 section version

[Section]
1 Section
2 First stage
65 Last stage
8 Mass transfer coefficient BRF-85 = 1 5 1 0
1 Liquid phase resistance Included
2 Vapor flow Plug = 1 5 3 0
2 Liquid flow Plug = 1 5 4 0
7 Pressure drop SBF-89 = 1 5 2 0
1 Entrainment None = 1 2 5 0
1 Holdup Default = 1 5 6 0
1 Design method %flood = 1 5 10 2 * 0.5
5 Column internals Structured packing
1.2192 Column diameter
1.167454 Total tray area
3.2 Packing height
492 Specific packing surface
Sulzer BX SS
0.9 Void fraction
0.0127 Channel base
0.0064 Crimp height
0.0089 Channel side
0.00897 Equivalent diameter
1.047197 Channel flow angle
69 Packing factor
3.38 Parameter C3
15 Parameter C1
2 Parameter C2
0.28 Parameter C3
* Rivulet split parameter
* Parameter Ch
* Parameter Cp
* Parameter Cfl
0.66 Parameter Cl
0.22 Parameter Cv
* Flood P
1.25 Parameter K2
0.259 Parameter Fse
0.9 Parameter CE

[Pressures]
4 Column pressure Estimated pressure drop
97325.3 Condenser pressure
97325.3 Top pressure
393 Pressure Drop
* Bottom pressure

[Feeds]
1 Number
1 Feed state T & p
65 Stage Feed1
* Temperature
* Pressure
0 Vapour fraction
2 componentflows
0.0002 Component 1 flow
0.0008 Component 2 flow

[Condenser]
5 Type Reflux flow rate
0.009 Value Qcondenser
0 Subcooling
*  Type *
* Initialization guess

[Reboiler]
4 Type Bottom product flow rate
0 Value Qreboiler
*  Type *
* Initialization guess

[Solve options]
1 Initialization Automatic
1 Method Newton's method
0.5 Flow Step limit
10 Temperature Step limit
1 Composition 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
0 Interactive

[Programs]
Temporary file=SCRATCH.TMP
User program=
8 DOS extender NT
*  Show windows *

[FlowSheet]
<?xml version="1.0" encoding="UTF-8" standalone="no"?>
<!-- Created with ChemSep (http://www.chemsep.org/) --> 
<!DOCTYPE svg PUBLIC "-//W3C//DTD SVG 1.0//EN" "http://www.w3.org/TR/2001/PR-SVG-20010719/DTD/svg10.dtd">
<svg
   xmlns:svg="http://www.w3.org/2000/svg"
   xmlns="http://www.w3.org/2000/svg"
   version="1.0"
   x="0.0"
   y="0.0"
   width="1.0"
   height="1.0">
<penwidth>1</penwidth>
<move2 x=0 y=0 />
<move2 x=0 y=0 />
<line2 x=1 y=0 />
<line2 x=1 y=1 />
<line2 x=0 y=1 />
<line2 x=0 y=0 />
<move2 x=0.35 y=0.3 />
<line2 x=0.35 y=0.7 />
<penstyle>Dot</penstyle>
<move2 x=0.35 y=0.7 />
<line2 x=0.55 y=0.7 />
<penstyle>Solid</penstyle>
<move2 x=0.55 y=0.7 />
<line2 x=0.55 y=0.3 />
<penstyle>Dot</penstyle>
<move2 x=0.55 y=0.3 />
<line2 x=0.35 y=0.3 />
<penstyle>Solid</penstyle>
<string x=0.438679 y=0.724528 s="2" />
<arc x1=0.35 y1=0.75 x2=0.55 y2=0.65 x3=0.55 y3=0.7 x4=0.35 y4=0.7 />
<string x=0.427358 y=0.324528 s="65" />
<arc x1=0.35 y1=0.35 x2=0.55 y2=0.25 x3=0.35 y3=0.3 x4=0.55 y4=0.3 />
<move2 x=0.45 y=0.75 />
<line2 x=0.45 y=0.825 />
<move2 x=0.45 y=0.825 />
<line2 x=0.625 y=0.825 />
<line2 x=0.605 y=0.835 />
<line2 x=0.605 y=0.815 />
<line2 x=0.625 y=0.825 />
<move2 x=0.7 y=0.75 />
<line2 x=0.7 y=0.7 />
<move2 x=0.7 y=0.7 />
<line2 x=0.55 y=0.7 />
<line2 x=0.57 y=0.69 />
<line2 x=0.57 y=0.71 />
<line2 x=0.55 y=0.7 />
<arc x1=0.625 y1=0.9 x2=0.775 y2=0.75 x3=0.7 y3=0.9 x4=0.7 y4=0.9 />
<string x=0.7 y=0.825 s="1" />
<move2 x=0.775 y=0.9 />
<line2 x=0.625 y=0.75 />
<line2 x=0.646213 y=0.757071 />
<move2 x=0.625 y=0.75 />
<line2 x=0.632071 y=0.771213 />
<move2 x=0.55 y=0.7 />
<line2 x=0.9 y=0.7 />
<line2 x=0.88 y=0.71 />
<line2 x=0.88 y=0.69 />
<line2 x=0.9 y=0.7 />
<string x=0.828302 y=0.769057 s="Top" />
<move2 x=0.45 y=0.25 />
<line2 x=0.45 y=0.175 />
<move2 x=0.45 y=0.175 />
<line2 x=0.625 y=0.175 />
<line2 x=0.605 y=0.185 />
<line2 x=0.605 y=0.165 />
<line2 x=0.625 y=0.175 />
<move2 x=0.7 y=0.25 />
<line2 x=0.7 y=0.3 />
<move2 x=0.7 y=0.3 />
<line2 x=0.55 y=0.3 />
<line2 x=0.57 y=0.29 />
<line2 x=0.57 y=0.31 />
<line2 x=0.55 y=0.3 />
<arc x1=0.625 y1=0.25 x2=0.775 y2=0.1 x3=0.7 y3=0.25 x4=0.7 y4=0.25 />
<string x=0.7 y=0.175 s="66" />
<move2 x=0.625 y=0.1 />
<line2 x=0.775 y=0.25 />
<line2 x=0.753787 y=0.242929 />
<move2 x=0.775 y=0.25 />
<line2 x=0.767929 y=0.228787 />
<move2 x=0.55 y=0.3 />
<line2 x=0.9 y=0.3 />
<line2 x=0.88 y=0.31 />
<line2 x=0.88 y=0.29 />
<line2 x=0.9 y=0.3 />
<string x=0.775472 y=0.369057 s="Bottom" />
</svg>

[CoCo]
<icon>
# Coco icon generated by ChemSep
# Sizes
WIDTH           14
HEIGHT          20
DEFHEIGHT       24
XGROW           4
YGROW           10
# column + Internals
BODY            0 4 8 16 -1 4
LINE            DASHED 0.5 8 7.5  8
LINE            DASHED 0.5 12 7.5 12
# Total Subcooled Condenser
BODY            10 0 14 4 -1 -1
LINE            4 4 4 2
LINE            ARROW 4 2 10 2
LINE            12 4 12 8
LINE            ARROW 12 8 8 8
LINE            THINLINE OARROW 14.2 -.2 9.8 4.2
LINE            12 8 14 8
CONNECTION      14 8
# Total Reboiler
BODY            10 16 14 20 -1 -1
LINE            4 16 4 18
LINE            ARROW 4 18 10 18
LINE            12 16 12 12
LINE            ARROW 12 12 8 12
LINE            THINLINE OARROW 9.8 20.2 14.2 15.8
LINE            12 12 14 12
CONNECTION      14 12
# Connections and free space for feeds and sidestreams
VCONNECTION     0 8 12
VCONNECTION     8 9 11
FREESPACE       9 9 12 11
FREESPACE       13 9 14 11
</icon>

[Settings]
<Graphs>
-1
-1
-1
1 Graph settings
1 Auto colors
1 Auto points
0.2
StringGrid5
2
8
Title
Labels
Stages
Axis color
Commands
Box
Labels box
Import data
Sulzer BX o/p-Xylene 730 Torr @ FRI (1.22m ID) CEPjan1998p60fig1a
On
Vertical
Black
set label "ChemSep" at 3,0.3 right
On
Off
Z:\big\cs\databases\howto_distillation\howto_distillation.txt
StringGrid4
5
9

Title
Start
End
Tic interval
Small tics
Grid
Logarithmic
Scientific notation
x1
F-factor
0
3
1
4
Off
Off
Off
y1
Average HETP (m)
0
0.3
0.05
4
Off
Off
Off
x2




0
Off
Off
Off
y2




0
Off
Off
Off
StringGrid3
2
14

Label
Plot X
Plot Y
X axis
Y axis
Units X
Units Y
Color
Points
Thickness
Style
1st stage
Last stage
5
BRF85
PS2
PS3
x1
y1


Green
No Points
Normal
Solid
1
6
</Graphs>
<McCabe-Thiele>
0 Graph settings
1
0
StringGrid7
16
2
Title
McCabe-Thiele diagram for P-xylene - O-xylene
Xlabel
X P-xylene/(P-xylene+O-xylene)
Ylabel
Y P-xylene/(P-xylene+O-xylene)
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
StringGrid11
5
3















</McCabe-Thiele>
<FUG>
1
0
0
0.95
0.95
1.2
</FUG>
<Parametrix>
6
0 Use old results
1 Automatic
0 Keep sep-files
1 Restore original
StringGrid1
2
6
Name
Variable
Units
Value
Start/Valuelist
End
Reflux liquid flowrate (mol/s)
RL
mol/s
9
5
50
StringGrid2
4
5
Name
Reflux liquid flowrate (mol/s)
F-factor
AHETP1
pd (mbar/m)
Variable
RL
FFAC35
AHETP1
(P44-P43)/Z43
Units
mol/s



Current Value
9
3.129096
0.316537
5.3125
StringGrid3
8
5
Step
Reflux liquid flowrate (mol/s)
F-factor
AHETP1
pd (mbar/m)
Units
mol/s



1
5
0.260999
0.123057
5.3125
2
14
0.73056
0.149537
30.15625
3
23
1.199758
0.165724
76.25
4
32
1.66839
0.178319
146.25
5
41
2.136184
0.188925
243.9062
6
50
2.602781
0.19822
375.3125
</Parametrix>
<BinaryPhaseDiagram>
-1
-1
-1

21

</BinaryPhaseDiagram>
[End Settings]

[End of Input]

[Results]
1 Converged
3 Iterations

[Profiles]

 Stage  Temperature  Pressure   Vapor Flow  Liquid Flow Vap Enthalpy Liq Enthalpy

   1    410.0238      97325.3   1.5625E-12        0.009  -2.036972E+07  -2.036972E+07
   2    410.0257      97325.3        0.009   0.00899988  1.555378E+07  -2.036937E+07
   3    410.0281        97326   0.00899988   0.00899977  1.555462E+07  -2.03689E+07
   4    410.0307      97326.7   0.00899977   0.00899966  1.55555E+07  -2.03684E+07
   5    410.0334     97327.39   0.00899966   0.00899955  1.555644E+07  -2.036787E+07
   6    410.0363     97328.09   0.00899955   0.00899943  1.555743E+07  -2.036732E+07
   7    410.0393     97328.78   0.00899943    0.0089993  1.555847E+07  -2.036673E+07
   8    410.0425     97329.48    0.0089993   0.00899916  1.555957E+07  -2.036612E+07
   9    410.0458     97330.18   0.00899916   0.00899902  1.556073E+07  -2.036547E+07
  10    410.0493     97330.88   0.00899902   0.00899886  1.556196E+07  -2.036479E+07
  11    410.0531     97331.57   0.00899886    0.0089987  1.556325E+07  -2.036407E+07
  12     410.057     97332.27    0.0089987   0.00899853  1.556462E+07  -2.036331E+07
  13    410.0611     97332.96   0.00899853   0.00899835  1.556606E+07  -2.036251E+07
  14    410.0654     97333.66   0.00899835   0.00899815  1.556758E+07  -2.036167E+07
  15      410.07     97334.36   0.00899815   0.00899795  1.556919E+07  -2.036079E+07
  16    410.0748     97335.05   0.00899795   0.00899773  1.557089E+07  -2.035986E+07
  17    410.0799     97335.75   0.00899773   0.00899751  1.557268E+07  -2.035888E+07
  18    410.0853     97336.45   0.00899751   0.00899726  1.557458E+07  -2.035784E+07
  19    410.0909     97337.14   0.00899726   0.00899701  1.557658E+07  -2.035675E+07
  20    410.0969     97337.84   0.00899701   0.00899674  1.557869E+07  -2.03556E+07
  21    410.1032     97338.53   0.00899674   0.00899645  1.558091E+07  -2.035439E+07
  22    410.1098     97339.23   0.00899645   0.00899615  1.558327E+07  -2.035311E+07
  23    410.1168     97339.93   0.00899615   0.00899583  1.558575E+07  -2.035176E+07
  24    410.1242     97340.63   0.00899583    0.0089955  1.558837E+07  -2.035034E+07
  25    410.1319     97341.32    0.0089955   0.00899514  1.559113E+07  -2.034884E+07
  26    410.1401     97342.02   0.00899514   0.00899477  1.559405E+07  -2.034726E+07
  27    410.1488     97342.71   0.00899477   0.00899437  1.559713E+07  -2.03456E+07
  28    410.1579     97343.41   0.00899437   0.00899395  1.560038E+07  -2.034384E+07
  29    410.1675      97344.1   0.00899395   0.00899351  1.560381E+07  -2.034199E+07
  30    410.1776      97344.8   0.00899351   0.00899305  1.560742E+07  -2.034004E+07
  31    410.1883      97345.5   0.00899305   0.00899256  1.561123E+07  -2.033798E+07
  32    410.1995      97346.2   0.00899256   0.00899204  1.561526E+07  -2.033581E+07
  33    410.2114     97346.89   0.00899204   0.00899149  1.561949E+07  -2.033352E+07
  34    410.2238     97347.59   0.00899149   0.00899092  1.562396E+07  -2.033112E+07
  35     410.237     97348.28   0.00899092   0.00899031  1.562867E+07  -2.032858E+07
  36    410.2508     97348.98   0.00899031   0.00898967  1.563363E+07  -2.03259E+07
  37    410.2654     97349.67   0.00898967     0.008989  1.563886E+07  -2.032309E+07
  38    410.2808     97350.37     0.008989   0.00898829  1.564436E+07  -2.032012E+07
  39    410.2969     97351.06   0.00898829   0.00898755  1.565016E+07  -2.031699E+07
  40     410.314     97351.76   0.00898755   0.00898677  1.565626E+07  -2.031371E+07
  41    410.3319     97352.45   0.00898677   0.00898595  1.566267E+07  -2.031024E+07
  42    410.3507     97353.16   0.00898595   0.00898509  1.566943E+07  -2.03066E+07
  43    410.3705     97353.85   0.00898509   0.00898418  1.567653E+07  -2.030277E+07
  44    410.3914     97354.55   0.00898418   0.00898323  1.568399E+07  -2.029873E+07
  45    410.4132     97355.24   0.00898323   0.00898223  1.569184E+07  -2.029449E+07
  46    410.4362     97355.94   0.00898223   0.00898118  1.570007E+07  -2.029004E+07
  47    410.4604     97356.63   0.00898118   0.00898009  1.570873E+07  -2.028536E+07
  48    410.4857     97357.33   0.00898009   0.00897894  1.571781E+07  -2.028044E+07
  49    410.5124     97358.02   0.00897894   0.00897773  1.572733E+07  -2.027527E+07
  50    410.5403     97358.72   0.00897773   0.00897648  1.573732E+07  -2.026985E+07
  51    410.5695     97359.41   0.00897648   0.00897516  1.574778E+07  -2.026416E+07
  52    410.6002     97360.11   0.00897516   0.00897379  1.575874E+07  -2.02582E+07
  53    410.6324      97360.8   0.00897379   0.00897236  1.577021E+07  -2.025194E+07
  54     410.666      97361.5   0.00897236   0.00897087  1.57822E+07  -2.024539E+07
  55    410.7012      97362.2   0.00897087   0.00896932  1.579474E+07  -2.023854E+07
  56    410.7379     97362.89   0.00896932   0.00896771  1.580782E+07  -2.023136E+07
  57    410.7764     97363.58   0.00896771   0.00896605  1.582147E+07  -2.022385E+07
  58    410.8165     97364.27   0.00896605   0.00896432  1.583569E+07  -2.0216E+07
  59    410.8584     97364.97   0.00896432   0.00896254  1.585048E+07  -2.02078E+07
  60    410.9021     97365.66   0.00896254   0.00896072  1.586583E+07  -2.019924E+07
  61    410.9476     97366.36   0.00896072   0.00895885  1.588174E+07  -2.019032E+07
  62     410.995     97367.05   0.00895885   0.00895696  1.589818E+07  -2.018101E+07
  63    411.0443     97367.75   0.00895696   0.00895506  1.59151E+07  -2.017132E+07
  64    411.0956     97368.45   0.00895506   0.00895318  1.593244E+07  -2.016124E+07
  65    411.1488     97369.13   0.00895318   0.00895137  1.59501E+07  -2.015075E+07
  66    411.3174     97369.83   0.00895137   1.5625E-12  1.596791E+07  1.596791E+07

[Enthalpies/Entropies]

 Stage  Vap.Enthalpy    Liq.Enthalpy    Vap.Entropy       Liq.Entropy

   1 -2.036972E+07  -2.036972E+07     44623.42    -42942.71
   2 1.555378E+07  -2.036937E+07     44670.48    -42925.89
   3 1.555462E+07  -2.03689E+07     44688.03    -42908.01
   4 1.55555E+07  -2.03684E+07     44706.42    -42889.26
   5 1.555644E+07  -2.036787E+07     44725.68    -42869.64
   6 1.555743E+07  -2.036732E+07     44745.84     -42849.1
   7 1.555847E+07  -2.036673E+07     44766.95    -42827.62
   8 1.555957E+07  -2.036612E+07     44789.04    -42805.14
   9 1.556073E+07  -2.036547E+07     44812.17    -42781.64
  10 1.556196E+07  -2.036479E+07     44836.37    -42757.05
  11 1.556325E+07  -2.036407E+07     44861.69    -42731.36
  12 1.556462E+07  -2.036331E+07     44888.18    -42704.49
  13 1.556606E+07  -2.036251E+07     44915.89    -42676.41
  14 1.556758E+07  -2.036167E+07     44944.85    -42647.07
  15 1.556919E+07  -2.036079E+07     44975.14    -42616.42
  16 1.557089E+07  -2.035986E+07      45006.8    -42584.41
  17 1.557268E+07  -2.035888E+07     45039.88    -42550.98
  18 1.557458E+07  -2.035784E+07     45074.45    -42516.07
  19 1.557658E+07  -2.035675E+07     45110.56    -42479.64
  20 1.557869E+07  -2.03556E+07     45148.27    -42441.63
  21 1.558091E+07  -2.035439E+07     45187.64    -42401.96
  22 1.558327E+07  -2.035311E+07     45228.73     -42360.6
  23 1.558575E+07  -2.035176E+07     45271.62    -42317.47
  24 1.558837E+07  -2.035034E+07     45316.36    -42272.51
  25 1.559113E+07  -2.034884E+07     45363.02    -42225.66
  26 1.559405E+07  -2.034726E+07     45411.67    -42176.86
  27 1.559713E+07  -2.03456E+07     45462.38    -42126.04
  28 1.560038E+07  -2.034384E+07     45515.21    -42073.14
  29 1.560381E+07  -2.034199E+07     45570.25    -42018.08
  30 1.560742E+07  -2.034004E+07     45627.55    -41960.81
  31 1.561123E+07  -2.033798E+07      45687.2    -41901.25
  32 1.561526E+07  -2.033581E+07     45749.26    -41839.35
  33 1.561949E+07  -2.033352E+07      45813.8    -41775.03
  34 1.562396E+07  -2.033112E+07     45880.91    -41708.24
  35 1.562867E+07  -2.032858E+07     45950.64     -41638.9
  36 1.563363E+07  -2.03259E+07     46023.07    -41566.97
  37 1.563886E+07  -2.032309E+07     46098.27    -41492.36
  38 1.564436E+07  -2.032012E+07      46176.3    -41415.04
  39 1.565016E+07  -2.031699E+07     46257.24    -41334.94
  40 1.565626E+07  -2.031371E+07     46341.13    -41252.01
  41 1.566267E+07  -2.031024E+07     46428.06     -41166.2
  42 1.566943E+07  -2.03066E+07     46518.05    -41077.46
  43 1.567653E+07  -2.030277E+07     46611.19    -40985.77
  44 1.568399E+07  -2.029873E+07     46707.49    -40891.08
  45 1.569184E+07  -2.029449E+07     46807.02    -40793.36
  46 1.570007E+07  -2.029004E+07     46909.81     -40692.6
  47 1.570873E+07  -2.028536E+07     47015.88    -40588.78
  48 1.571781E+07  -2.028044E+07     47125.25    -40481.89
  49 1.572733E+07  -2.027527E+07     47237.94    -40371.93
  50 1.573732E+07  -2.026985E+07     47353.95    -40258.93
  51 1.574778E+07  -2.026416E+07     47473.28     -40142.9
  52 1.575874E+07  -2.02582E+07     47595.89    -40023.87
  53 1.577021E+07  -2.025194E+07     47721.77     -39901.9
  54 1.57822E+07  -2.024539E+07     47850.86    -39777.05
  55 1.579474E+07  -2.023854E+07     47983.09    -39649.39
  56 1.580782E+07  -2.023136E+07      48118.4       -39519
  57 1.582147E+07  -2.022385E+07     48256.67       -39386
  58 1.583569E+07  -2.0216E+07     48397.79    -39250.51
  59 1.585048E+07  -2.02078E+07      48541.6    -39112.66
  60 1.586583E+07  -2.019924E+07     48687.92     -38972.6
  61 1.588174E+07  -2.019032E+07     48836.53    -38830.52
  62 1.589818E+07  -2.018101E+07     48987.16    -38686.61
  63 1.59151E+07  -2.017132E+07     49139.48    -38541.07
  64 1.593244E+07  -2.016124E+07      49293.1    -38394.14
  65 1.59501E+07  -2.015075E+07     49447.49    -38246.06
  66 1.596791E+07  1.596791E+07     49602.02    -37817.27

[Temperatures]

 Stage  Interface       Liquid    Bubble pt        Vapor       Dew pt

   1     410.0238     410.0238     410.0238     410.0238     410.0238
   2     410.0259     410.0257     410.0259     410.0325     410.0327
   3     410.0284     410.0281     410.0284     410.0353     410.0356
   4      410.031     410.0307      410.031     410.0383     410.0386
   5     410.0338     410.0334     410.0338     410.0414     410.0417
   6     410.0367     410.0363     410.0367     410.0447     410.0451
   7     410.0397     410.0393     410.0397     410.0482     410.0486
   8     410.0429     410.0425     410.0429     410.0518     410.0523
   9     410.0463     410.0458     410.0462     410.0557     410.0562
  10     410.0498     410.0493     410.0498     410.0598     410.0604
  11     410.0535     410.0531     410.0535      410.064     410.0647
  12     410.0575      410.057     410.0575     410.0685     410.0693
  13     410.0616     410.0611     410.0616     410.0733     410.0741
  14      410.066     410.0654      410.066     410.0783     410.0792
  15     410.0706       410.07     410.0706     410.0836     410.0846
  16     410.0755     410.0748     410.0754     410.0891     410.0902
  17     410.0806     410.0799     410.0805      410.095     410.0962
  18      410.086     410.0853     410.0859     410.1011     410.1025
  19     410.0917     410.0909     410.0916     410.1077     410.1091
  20     410.0977     410.0969     410.0976     410.1145     410.1161
  21      410.104     410.1032      410.104     410.1218     410.1235
  22     410.1107     410.1098     410.1106     410.1294     410.1312
  23     410.1177     410.1168     410.1176     410.1375     410.1394
  24     410.1251     410.1242     410.1251     410.1459      410.148
  25     410.1329     410.1319     410.1329     410.1549     410.1572
  26     410.1412     410.1401     410.1411     410.1643     410.1667
  27     410.1499     410.1488     410.1498     410.1743     410.1769
  28      410.159     410.1579      410.159     410.1848     410.1875
  29     410.1687     410.1675     410.1687     410.1958     410.1988
  30     410.1789     410.1776     410.1788     410.2074     410.2106
  31     410.1896     410.1883     410.1896     410.2197     410.2231
  32     410.2009     410.1995     410.2009     410.2326     410.2362
  33     410.2129     410.2114     410.2128     410.2462     410.2501
  34     410.2254     410.2238     410.2254     410.2605     410.2647
  35     410.2387      410.237     410.2386     410.2756       410.28
  36     410.2526     410.2508     410.2525     410.2915     410.2962
  37     410.2673     410.2654     410.2672     410.3082     410.3132
  38     410.2827     410.2808     410.2827     410.3257     410.3311
  39      410.299     410.2969      410.299     410.3442     410.3499
  40     410.3162      410.314     410.3161     410.3636     410.3697
  41     410.3342     410.3319     410.3341     410.3841     410.3905
  42     410.3531     410.3507     410.3531     410.4055     410.4124
  43     410.3731     410.3705      410.373     410.4281     410.4353
  44      410.394     410.3914     410.3939     410.4518     410.4595
  45      410.416     410.4132      410.416     410.4767     410.4848
  46     410.4392     410.4362     410.4391     410.5027     410.5114
  47     410.4635     410.4604     410.4634     410.5301     410.5392
  48      410.489     410.4857     410.4889     410.5587     410.5685
  49     410.5158     410.5124     410.5157     410.5888     410.5991
  50     410.5439     410.5403     410.5437     410.6202     410.6311
  51     410.5733     410.5695     410.5732     410.6531     410.6647
  52     410.6042     410.6002      410.604     410.6875     410.6998
  53     410.6365     410.6324     410.6363     410.7234     410.7365
  54     410.6703      410.666     410.6701      410.761     410.7748
  55     410.7057     410.7012     410.7055        410.8     410.8148
  56     410.7427     410.7379     410.7425     410.8408     410.8566
  57     410.7813     410.7764     410.7812     410.8831     410.9002
  58     410.8217     410.8165     410.8215     410.9271     410.9456
  59     410.8638     410.8584     410.8636     410.9726     410.9928
  60     410.9077     410.9021     410.9075     411.0196      411.042
  61     410.9535     410.9476     410.9533     411.0679      411.093
  62     411.0011      410.995     411.0009     411.1174     411.1461
  63     411.0507     411.0443     411.0504     411.1676     411.2011
  64     411.1022     411.0956     411.1019     411.2183     411.2581
  65     411.1557     411.1488     411.1554     411.2685     411.3171
  66     411.3174     411.3174     411.3174     411.3174     411.3174

[Vapour phase compositions]

 Component    Vapour phase compositions on stage   1 to   5

     1   0.00534203   0.00629694   0.00666517   0.00705479   0.00746703  
     2     0.994658     0.993703     0.993335     0.992945     0.992533  

 Component    Vapour phase compositions on stage   6 to  10

     1   0.00790318    0.0083646   0.00885275   0.00936912   0.00991534  
     2     0.992097     0.991635     0.991147     0.990631     0.990085  

 Component    Vapour phase compositions on stage  11 to  15

     1    0.0104931    0.0111042    0.0117504    0.0124339    0.0131566  
     2     0.989507     0.988896      0.98825     0.987566     0.986843  

 Component    Vapour phase compositions on stage  16 to  20

     1    0.0139207    0.0147286    0.0155827    0.0164856      0.01744  
     2     0.986079     0.985271     0.984417     0.983514      0.98256  

 Component    Vapour phase compositions on stage  21 to  25

     1    0.0184486    0.0195144    0.0206407    0.0218306    0.0230876  
     2     0.981551     0.980486     0.979359     0.978169     0.976912  

 Component    Vapour phase compositions on stage  26 to  30

     1    0.0244153    0.0258175    0.0272982    0.0288614    0.0305115  
     2     0.975585     0.974182     0.972702     0.971139     0.969488  

 Component    Vapour phase compositions on stage  31 to  35

     1    0.0322531    0.0340908    0.0360296    0.0380746    0.0402312  
     2     0.967747     0.965909      0.96397     0.961925     0.959769  

 Component    Vapour phase compositions on stage  36 to  40

     1    0.0425049    0.0449016    0.0474271    0.0500878    0.0528901  
     2     0.957495     0.955098     0.952573     0.949912      0.94711  

 Component    Vapour phase compositions on stage  41 to  45

     1    0.0558405     0.058946    0.0622137    0.0656506    0.0692645  
     2     0.944159     0.941054     0.937786     0.934349     0.930736  

 Component    Vapour phase compositions on stage  46 to  50

     1    0.0730627    0.0770531    0.0812437    0.0856425    0.0902576  
     2     0.926937     0.922947     0.918756     0.914357     0.909742  

 Component    Vapour phase compositions on stage  51 to  55

     1    0.0950973      0.10017     0.105483     0.111046     0.116867  
     2     0.904903      0.89983     0.894517     0.888954     0.883133  

 Component    Vapour phase compositions on stage  56 to  60

     1     0.122953     0.129312     0.135953     0.142883     0.150108  
     2     0.877047     0.870688     0.864047     0.857117     0.849892  

 Component    Vapour phase compositions on stage  61 to  65

     1     0.157635     0.165471      0.17362     0.182089     0.190881  
     2     0.842365     0.834529      0.82638     0.817911     0.809119  

 Component    Vapour phase compositions on stage  66 to  66

     1          0.2  
     2          0.8  

[Liquid phase compositions]

 Component    Liquid phase compositions on stage   1 to   5

     1   0.00629694   0.00666517   0.00705479   0.00746703   0.00790318  
     2     0.993703     0.993335     0.992945     0.992533     0.992097  

 Component    Liquid phase compositions on stage   6 to  10

     1    0.0083646   0.00885275   0.00936912   0.00991534    0.0104931  
     2     0.991635     0.991147     0.990631     0.990085     0.989507  

 Component    Liquid phase compositions on stage  11 to  15

     1    0.0111042    0.0117504    0.0124339    0.0131566    0.0139207  
     2     0.988896      0.98825     0.987566     0.986843     0.986079  

 Component    Liquid phase compositions on stage  16 to  20

     1    0.0147286    0.0155827    0.0164856      0.01744    0.0184486  
     2     0.985271     0.984417     0.983514      0.98256     0.981551  

 Component    Liquid phase compositions on stage  21 to  25

     1    0.0195144    0.0206407    0.0218306    0.0230876    0.0244153  
     2     0.980486     0.979359     0.978169     0.976912     0.975585  

 Component    Liquid phase compositions on stage  26 to  30

     1    0.0258175    0.0272982    0.0288614    0.0305115    0.0322531  
     2     0.974182     0.972702     0.971139     0.969488     0.967747  

 Component    Liquid phase compositions on stage  31 to  35

     1    0.0340908    0.0360296    0.0380746    0.0402312    0.0425049  
     2     0.965909      0.96397     0.961925     0.959769     0.957495  

 Component    Liquid phase compositions on stage  36 to  40

     1    0.0449016    0.0474271    0.0500878    0.0528901    0.0558405  
     2     0.955098     0.952573     0.949912      0.94711     0.944159  

 Component    Liquid phase compositions on stage  41 to  45

     1     0.058946    0.0622137    0.0656506    0.0692645    0.0730627  
     2     0.941054     0.937786     0.934349     0.930736     0.926937  

 Component    Liquid phase compositions on stage  46 to  50

     1    0.0770531    0.0812437    0.0856425    0.0902576    0.0950973  
     2     0.922947     0.918756     0.914357     0.909742     0.904903  

 Component    Liquid phase compositions on stage  51 to  55

     1      0.10017     0.105483     0.111046     0.116867     0.122953  
     2      0.89983     0.894517     0.888954     0.883133     0.877047  

 Component    Liquid phase compositions on stage  56 to  60

     1     0.129312     0.135953     0.142883     0.150108     0.157635  
     2     0.870688     0.864047     0.857117     0.849892     0.842365  

 Component    Liquid phase compositions on stage  61 to  65

     1     0.165471      0.17362     0.182089     0.190881          0.2  
     2     0.834529      0.82638     0.817911     0.809119          0.8  

 Component    Liquid phase compositions on stage  66 to  66

     1     0.227643  
     2     0.772357  

[Interface vapour mole fractions]

 Component    Interface vapour mole fractions on stage   1 to   5

     1   0.00534203    0.0056562    0.0059872   0.00633747   0.00670809  
     2     0.994658     0.994344     0.994013     0.993663     0.993292  

 Component    Interface vapour mole fractions on stage   6 to  10

     1   0.00710026   0.00751519   0.00795419   0.00841864   0.00890998  
     2       0.9929     0.992485     0.992046     0.991581      0.99109  

 Component    Interface vapour mole fractions on stage  11 to  15

     1   0.00942976   0.00997958    0.0105611    0.0111762    0.0118268  
     2      0.99057      0.99002     0.989439     0.988824     0.988173  

 Component    Interface vapour mole fractions on stage  16 to  20

     1    0.0125148    0.0132423    0.0140115    0.0148248    0.0156847  
     2     0.987485     0.986758     0.985988     0.985175     0.984315  

 Component    Interface vapour mole fractions on stage  21 to  25

     1    0.0165936    0.0175544    0.0185699     0.019643    0.0207769  
     2     0.983406     0.982446      0.98143     0.980357     0.979223  

 Component    Interface vapour mole fractions on stage  26 to  30

     1     0.021975    0.0232406    0.0245775    0.0259894    0.0274803  
     2     0.978025     0.976759     0.975423     0.974011      0.97252  

 Component    Interface vapour mole fractions on stage  31 to  35

     1    0.0290544    0.0307161      0.03247    0.0343207    0.0362733  
     2     0.970946     0.969284      0.96753     0.965679     0.963727  

 Component    Interface vapour mole fractions on stage  36 to  40

     1     0.038333    0.0405051    0.0427953    0.0452094    0.0477535  
     2     0.961667     0.959495     0.957205     0.954791     0.952246  

 Component    Interface vapour mole fractions on stage  41 to  45

     1    0.0504338    0.0532569    0.0562294    0.0593583    0.0626507  
     2     0.949566     0.946743     0.943771     0.940642     0.937349  

 Component    Interface vapour mole fractions on stage  46 to  50

     1    0.0661139    0.0697555    0.0735832    0.0776048    0.0818284  
     2     0.933886     0.930244     0.926417     0.922395     0.918172  

 Component    Interface vapour mole fractions on stage  51 to  55

     1    0.0862621     0.090914    0.0957927     0.100906     0.106263  
     2     0.913738     0.909086     0.904207     0.899094     0.893737  

 Component    Interface vapour mole fractions on stage  56 to  60

     1     0.111872     0.117741     0.123878     0.130291     0.136988  
     2     0.888128     0.882259     0.876122     0.869709     0.863012  

 Component    Interface vapour mole fractions on stage  61 to  65

     1     0.143976     0.151263     0.158855     0.166759     0.174979  
     2     0.856024     0.848737     0.841145     0.833241     0.825021  

 Component    Interface vapour mole fractions on stage  66 to  66

     1          0.2  
     2          0.8  

[Interface liquid mole fractions]

 Component    Interface liquid mole fractions on stage   1 to   5

     1   0.00629694   0.00666688    0.0070566   0.00746895   0.00790521  
     2     0.993703     0.993333     0.992943     0.992531     0.992095  

 Component    Interface liquid mole fractions on stage   6 to  10

     1   0.00836675   0.00885502   0.00937153   0.00991789    0.0104958  
     2     0.991633     0.991145     0.990628     0.990082     0.989504  

 Component    Interface liquid mole fractions on stage  11 to  15

     1     0.011107    0.0117534     0.012437    0.0131599    0.0139243  
     2     0.988893     0.988247     0.987563      0.98684     0.986076  

 Component    Interface liquid mole fractions on stage  16 to  20

     1    0.0147324    0.0155867    0.0164898    0.0174444    0.0184533  
     2     0.985268     0.984413      0.98351     0.982556     0.981547  

 Component    Interface liquid mole fractions on stage  21 to  25

     1    0.0195194     0.020646    0.0218362    0.0230935    0.0244215  
     2     0.980481     0.979354     0.978164     0.976906     0.975578  

 Component    Interface liquid mole fractions on stage  26 to  30

     1    0.0258241    0.0273051    0.0288687    0.0305192    0.0322612  
     2     0.974176     0.972695     0.971131     0.969481     0.967739  

 Component    Interface liquid mole fractions on stage  31 to  35

     1    0.0340994    0.0360387    0.0380842    0.0402413    0.0425156  
     2     0.965901     0.963961     0.961916     0.959759     0.957484  

 Component    Interface liquid mole fractions on stage  36 to  40

     1    0.0449128     0.047439    0.0501003    0.0529033    0.0558544  
     2     0.955087     0.952561       0.9499     0.947097     0.944146  

 Component    Interface liquid mole fractions on stage  41 to  45

     1    0.0589607    0.0622291    0.0656669    0.0692815    0.0730806  
     2     0.941039     0.937771     0.934333     0.930718     0.926919  

 Component    Interface liquid mole fractions on stage  46 to  50

     1     0.077072    0.0812636    0.0856634    0.0902795    0.0951203  
     2     0.922928     0.918736     0.914337      0.90972      0.90488  

 Component    Interface liquid mole fractions on stage  51 to  55

     1     0.100194     0.105509     0.111073     0.116895     0.122982  
     2     0.899806     0.894491     0.888927     0.883105     0.877018  

 Component    Interface liquid mole fractions on stage  56 to  60

     1     0.129343     0.135985     0.142916     0.150142     0.157671  
     2     0.870657     0.864015     0.857084     0.849858     0.842329  

 Component    Interface liquid mole fractions on stage  61 to  65

     1     0.165508      0.17366      0.18213     0.190924     0.200044  
     2     0.834492      0.82634      0.81787     0.809076     0.799956  

 Component    Interface liquid mole fractions on stage  66 to  66

     1     0.227643  
     2     0.772357  

[Murphree efficiencies]

 Component    Murphree efficiencies on stage   1 to   5

     1            1     0.364429     0.364428     0.364427     0.364426  
     2            1     0.364429     0.364428     0.364427     0.364426  

 Component    Murphree efficiencies on stage   6 to  10

     1     0.364425     0.364424     0.364423     0.364422      0.36442  
     2     0.364425     0.364424     0.364423     0.364422      0.36442  

 Component    Murphree efficiencies on stage  11 to  15

     1     0.364419     0.364417     0.364415     0.364414     0.364412  
     2     0.364419     0.364417     0.364415     0.364414     0.364412  

 Component    Murphree efficiencies on stage  16 to  20

     1      0.36441     0.364407     0.364405     0.364403       0.3644  
     2      0.36441     0.364407     0.364405     0.364403       0.3644  

 Component    Murphree efficiencies on stage  21 to  25

     1     0.364397     0.364394     0.364391     0.364388     0.364384  
     2     0.364397     0.364394     0.364391     0.364388     0.364384  

 Component    Murphree efficiencies on stage  26 to  30

     1      0.36438     0.364376     0.364372     0.364368     0.364363  
     2      0.36438     0.364376     0.364372     0.364368     0.364363  

 Component    Murphree efficiencies on stage  31 to  35

     1     0.364358     0.364353     0.364347     0.364341     0.364335  
     2     0.364358     0.364353     0.364347     0.364341     0.364335  

 Component    Murphree efficiencies on stage  36 to  40

     1     0.364329     0.364322     0.364314     0.364306     0.364298  
     2     0.364329     0.364322     0.364314     0.364306     0.364298  

 Component    Murphree efficiencies on stage  41 to  45

     1      0.36429      0.36428     0.364271     0.364261      0.36425  
     2      0.36429      0.36428     0.364271     0.364261      0.36425  

 Component    Murphree efficiencies on stage  46 to  50

     1     0.364239     0.364227     0.364214     0.364201     0.364187  
     2     0.364239     0.364227     0.364214     0.364201     0.364187  

 Component    Murphree efficiencies on stage  51 to  55

     1     0.364172     0.364157     0.364141     0.364124     0.364106  
     2     0.364172     0.364157     0.364141     0.364124     0.364106  

 Component    Murphree efficiencies on stage  56 to  60

     1     0.364087     0.364067     0.364047     0.364025     0.364002  
     2     0.364087     0.364067     0.364047     0.364025     0.364002  

 Component    Murphree efficiencies on stage  61 to  65

     1     0.363977     0.363952     0.363924     0.363895     0.363863  
     2     0.363977     0.363952     0.363924     0.363895     0.363863  

 Component    Murphree efficiencies on stage  66 to  66

     1            1  
     2            1  

[Fractionation efficiencies]

 Stage  Fractionation Eff.  Fractionation Angle

   1           0            0
   2    0.364429            0
   3    0.364428            0
   4    0.364427  1.490116E-08
   5    0.364426            0
   6    0.364425            0
   7    0.364424            0
   8    0.364423            0
   9    0.364422            0
  10     0.36442            0
  11    0.364419            0
  12    0.364417            0
  13    0.364415  1.490116E-08
  14    0.364413            0
  15    0.364412            0
  16     0.36441            0
  17    0.364407            0
  18    0.364405            0
  19    0.364403            0
  20      0.3644            0
  21    0.364397            0
  22    0.364394            0
  23    0.364391            0
  24    0.364388            0
  25    0.364384            0
  26     0.36438            0
  27    0.364376  1.490116E-08
  28    0.364372            0
  29    0.364368            0
  30    0.364363            0
  31    0.364358            0
  32    0.364353            0
  33    0.364347            0
  34    0.364341            0
  35    0.364335            0
  36    0.364329            0
  37    0.364322            0
  38    0.364314            0
  39    0.364307            0
  40    0.364298            0
  41     0.36429            0
  42     0.36428  1.490116E-08
  43    0.364271            0
  44    0.364261            0
  45     0.36425            0
  46    0.364239            0
  47    0.364227            0
  48    0.364214            0
  49    0.364201            0
  50    0.364187            0
  51    0.364172            0
  52    0.364157            0
  53    0.364141            0
  54    0.364124            0
  55    0.364106            0
  56    0.364087  1.490116E-08
  57    0.364067            0
  58    0.364047            0
  59    0.364025  2.107342E-08
  60    0.364002            0
  61    0.363977            0
  62    0.363952            0
  63    0.363924            0
  64    0.363895            0
  65    0.363863  1.490116E-08
  66           0            0

[Mass transfer rates]

 Component    Mass transfer rates on stage   1 to   5

     1            0  3.31325E-06  0.0000035058  3.70923E-06  3.92428E-06  
     2            0  -3.43584E-06  -3.61103E-06  -0.000003818  -4.03926E-06  

 Component    Mass transfer rates on stage   6 to  10

     1  0.0000041516  4.39185E-06  4.64577E-06  4.91409E-06  5.19759E-06  
     2  -4.27341E-06  -4.52093E-06  -4.78251E-06  -5.05893E-06  -5.35099E-06  

 Component    Mass transfer rates on stage  11 to  15

     1  0.0000054971  5.81348E-06  6.14763E-06  6.50051E-06  6.87309E-06  
     2  -5.65954E-06  -5.98546E-06  -6.32968E-06  -6.69317E-06  -7.07697E-06  

 Component    Mass transfer rates on stage  16 to  20

     1  7.26642E-06  7.68158E-06  0.0000081197  8.58196E-06  9.06958E-06  
     2  -7.48212E-06  -7.90975E-06  -8.36102E-06  -8.83714E-06  -9.33937E-06  

 Component    Mass transfer rates on stage  21 to  25

     1  9.58385E-06  0.0000101261  0.0000106977  0.0000113001  0.0000119348  
     2  -9.86904E-06  -0.0000104275  -0.0000110162  -0.0000116365  -0.0000122901  

 Component    Mass transfer rates on stage  26 to  30

     1  0.0000126033  0.0000133071  0.000014048  0.0000148276  0.0000156477  
     2  -0.0000129785  -0.0000137033  -0.0000144662  -0.0000152689  -0.0000161132  

 Component    Mass transfer rates on stage  31 to  35

     1  0.0000165099  0.0000174161  0.0000183682  0.0000193679  0.0000204172  
     2  -0.0000170008  -0.0000179338  -0.0000189138  -0.0000199429  -0.0000210229  

 Component    Mass transfer rates on stage  36 to  40

     1  0.000021518  0.0000226721  0.0000238815  0.0000251481  0.0000264737  
     2  -0.0000221559  -0.0000233437  -0.0000245882  -0.0000258915  -0.0000272554  

 Component    Mass transfer rates on stage  41 to  45

     1   0.00002786  0.000029309  0.0000308222  0.0000324012  0.0000340475  
     2  -0.0000286817  -0.0000301722  -0.0000317287  -0.0000333527  -0.0000350458  

 Component    Mass transfer rates on stage  46 to  50

     1  0.0000357625  0.0000375473  0.000039403  0.0000413302  0.0000433297  
     2  -0.0000368092  -0.0000386442  -0.0000405516  -0.0000425323  -0.0000445867  

 Component    Mass transfer rates on stage  51 to  55

     1  0.0000454015  0.0000475457  0.0000497619  0.0000520493  0.0000544069  
     2  -0.000046715  -0.0000489169  -0.0000511919  -0.000053539  -0.0000559566  

 Component    Mass transfer rates on stage  56 to  60

     1  0.000056833  0.0000593257  0.0000618824  0.0000645002  0.0000671757  
     2  -0.0000584425  -0.0000609941  -0.0000636076  -0.0000662788  -0.0000690019  

 Component    Mass transfer rates on stage  61 to  65

     1  0.0000699052  0.0000726845  0.0000755092  0.0000783753  0.0000812788  
     2  -0.0000717702  -0.0000745753  -0.0000774069  -0.0000802521  -0.0000830947  

 Component    Mass transfer rates on stage  66 to  66

     1            0  
     2            0  

[Reaction rates]

 Component    Reaction rates on stage   1 to   5

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage   6 to  10

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  11 to  15

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  16 to  20

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  21 to  25

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  26 to  30

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  31 to  35

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  36 to  40

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  41 to  45

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  46 to  50

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  51 to  55

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  56 to  60

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  61 to  65

     1            0            0            0            0            0  
     2            0            0            0            0            0  

 Component    Reaction rates on stage  66 to  66

     1            0  
     2            0  

[Condenser heat duty]
    -323311

[Reboiler heat duty]
     323311

[K-values]

 Component    K-values on stage   1 to   5

     1     0.848353     0.848402     0.848454     0.848509     0.848567  
     2      1.00096      1.00102      1.00108      1.00114      1.00121  

 Component    K-values on stage   6 to  10

     1     0.848628     0.848693     0.848761     0.848834      0.84891  
     2      1.00128      1.00135      1.00143      1.00151       1.0016  

 Component    K-values on stage  11 to  15

     1     0.848992     0.849077     0.849168     0.849264     0.849366  
     2       1.0017      1.00179       1.0019      1.00201      1.00213  

 Component    K-values on stage  16 to  20

     1     0.849473     0.849587     0.849707     0.849834     0.849968  
     2      1.00225      1.00238      1.00252      1.00267      1.00282  

 Component    K-values on stage  21 to  25

     1      0.85011     0.850259     0.850418     0.850585     0.850762  
     2      1.00298      1.00316      1.00334      1.00353      1.00374  

 Component    K-values on stage  26 to  30

     1     0.850949     0.851146     0.851354     0.851574     0.851807  
     2      1.00395      1.00418      1.00442      1.00467      1.00494  

 Component    K-values on stage  31 to  35

     1     0.852052     0.852311     0.852584     0.852872     0.853177  
     2      1.00522      1.00552      1.00584      1.00617      1.00652  

 Component    K-values on stage  36 to  40

     1     0.853497     0.853836     0.854192     0.854568     0.854964  
     2      1.00689      1.00728      1.00769      1.00812      1.00858  

 Component    K-values on stage  41 to  45

     1     0.855381      0.85582     0.856283      0.85677     0.857282  
     2      1.00906      1.00957       1.0101      1.01066      1.01125  

 Component    K-values on stage  46 to  50

     1      0.85782     0.858386     0.858981     0.859606     0.860263  
     2      1.01187      1.01253      1.01321      1.01393      1.01469  

 Component    K-values on stage  51 to  55

     1     0.860951     0.861674     0.862431     0.863225     0.864056  
     2      1.01548      1.01632      1.01719       1.0181      1.01906  

 Component    K-values on stage  56 to  60

     1     0.864927     0.865837     0.866789     0.867783      0.86882  
     2      1.02007      1.02112      1.02221      1.02336      1.02455  

 Component    K-values on stage  61 to  65

     1     0.869903     0.871031     0.872207      0.87343     0.874701  
     2       1.0258       1.0271      1.02846      1.02987      1.03133  

 Component    K-values on stage  66 to  66

     1     0.878568  
     2      1.03579  

[Molecular weights]

     1       106.167
     2       106.167

[Feed stream 1]

         65 Stage
          0 Flow rate
     298.15 Temperature [K]
     101325 Pressure [Pa]
-4.25434E+07 Enthalpy [J/kmol]
    -138531 Entropy [J/kmol/K]
          0 Vapour fraction [-]
          1 Liquid phase split ratio [-]
        0.2 Mole fraction of component  1
        0.8 Mole fraction of component  2
          0 Flow rate
        0.2 Mole fraction of component  1
        0.8 Mole fraction of component  2

[Top product]

          1 Stage
 1.5625E-12 Flow rate
    410.024 Temperature [K]
    97325.3 Pressure [Pa]
-2.03697E+07 Enthalpy [J/kmol]
   -42942.7 Entropy [J/kmol/K]
          0 Vapour fraction [-]
          1 Liquid phase split ratio [-]
 0.00629694 Mole fraction of component  1
   0.993703 Mole fraction of component  2
 1.5625E-12 Flow rate
 0.00629694 Mole fraction of component  1
   0.993703 Mole fraction of component  2

[Bottom product]

         66 Stage
 1.5625E-12 Flow rate
    411.317 Temperature [K]
    97369.8 Pressure [Pa]
1.59679E+07 Enthalpy [J/kmol]
      49602 Entropy [J/kmol/K]
          1 Vapour fraction [-]
          1 Liquid phase split ratio [-]
        0.2 Mole fraction of component  1
        0.8 Mole fraction of component  2
 1.5625E-12 Flow rate
        0.2 Mole fraction of component  1
        0.8 Mole fraction of component  2

[Designed Sections]
1 Number

[Section]
1 Section
2 First stage
65 Last stage
5 Column internals Structured packing
1.2192 Column diameter
1.167454 Total tray area
3.2 Packing height
492 Specific packing surface
Sulzer BX SS        
0.9 Void fraction
0.0127 Channel base
0.0064 Crimp height
0.0089 Channel side
0.00897 Equivalent diameter
1.0472 Channel flow angle
69 Packing factor
3.38 Parameter C3
15 Parameter C1
2 Parameter C2
0.28 Parameter C3
0.5 Rivulet split parameter
0.547 Parameter Ch
0.355 Parameter Cp
2.339 Parameter Cfl
0.66 Parameter Cl
0.22 Parameter Cv
1275.48 Flood P
1.25 Parameter K2
0.259 Parameter Fse
0.9 Parameter CE

[Operating Limits]

 Stage   FF      WF

    1           0            0
    2        0.12        0.092
    3        0.12        0.092
    4        0.12        0.092
    5        0.12        0.092
    6        0.12        0.092
    7        0.12        0.092
    8        0.12        0.092
    9        0.12        0.092
   10        0.12        0.092
   11        0.12        0.092
   12        0.12        0.092
   13        0.12        0.092
   14        0.12        0.092
   15        0.12        0.092
   16        0.12        0.092
   17        0.12        0.092
   18        0.12        0.092
   19        0.12        0.092
   20        0.12        0.092
   21        0.12        0.092
   22        0.12        0.092
   23        0.12        0.092
   24        0.12        0.092
   25        0.12        0.092
   26        0.12        0.092
   27        0.12        0.092
   28        0.12        0.092
   29        0.12        0.092
   30        0.12        0.092
   31        0.12        0.092
   32        0.12        0.092
   33        0.12        0.092
   34        0.12        0.092
   35        0.12        0.092
   36        0.12        0.092
   37        0.12        0.092
   38        0.12        0.092
   39        0.12        0.092
   40        0.12        0.092
   41        0.12        0.092
   42        0.12        0.092
   43        0.12        0.092
   44        0.12        0.092
   45        0.12        0.092
   46        0.12        0.092
   47        0.12        0.092
   48        0.12        0.092
   49        0.12        0.092
   50        0.12        0.092
   51        0.12        0.092
   52        0.12        0.092
   53        0.12        0.091
   54        0.12        0.091
   55        0.12        0.091
   56        0.12        0.091
   57        0.12        0.091
   58        0.12        0.091
   59        0.12        0.091
   60        0.12        0.091
   61        0.12        0.091
   62        0.12        0.091
   63        0.12        0.091
   64        0.12        0.091
   65        0.12        0.091
   66           0            0

[End of Results]