propylene
propane
PR
PR
1
0
0.01
0.40
h
1
0
original
0
sundials
1e-2
0
sundials
1e-2
1e-6
1e-2
2000
1000
20
1
1
1
1248
492
-94
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1
1
1248
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0
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simple_source
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276
0
68
30
streams
feed
simple_source
0
streams
Outlet
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stream
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NComp
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2
0
F
0
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0
kmol/h
T
0
323.15
0
K
P
0
20.4096
0
atm
h
0
-12826.4
0
kJ/kmol
v
0
0
0
z
0
0.4
0
1
0.6
0
PP
0
PP
0
NComp
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2
0
M
0
42.0804
0
kg/kmol
1
44.0962
0
kg/kmol
ValidPhases
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Vapour-Liquid
4
MolarComposition
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0.4
1
1
0.6
1
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1
0
F
0
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1
kmol/h
T
0
323.15
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K
T_Cdeg
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50
1
K
P
0
2068
1
kPa
PID
PIDT_reboiler
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1004
560
0
62.5
58
controllers/PIDs
PIDT_reboiler
PID
0
PID_Select
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Ideal_AW
4
Action
0
Reverse
4
Mode
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4
Clip
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Clipped
4
alpha
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0.2
4
beta
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1
4
bias
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0.5
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derivTime
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1
4
s
intTime
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10
4
s
gain
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3
4
gamma
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1
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tau
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4
s
tauSet
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1
4
s
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200
4
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400
4
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0
4
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Input
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331.763
0
Output
0
0.488341
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SetPoint
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(58+273)
1
PID
PIDL_sump
/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/PID.png
1109
463
0
62.5
58
controllers/PIDs
PIDL_sump
PID
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PID_Select
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Ideal_AW
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Action
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Direct
4
Mode
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Clip
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alpha
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1
4
beta
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bias
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0.2
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derivTime
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0
4
s
intTime
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2
4
min
gain
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5
4
gamma
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1
4
tau
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4
s
tauSet
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1
4
s
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0.1
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0.8
4
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0
4
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1
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Input
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0.699807
0
Output
0
1
0
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1
PID
PIDL_Condenser
/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/PID.png
1225
76
0
62.5
58
controllers/PIDs
PIDL_Condenser
PID
0
PID_Select
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Ideal_AW
4
Action
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Direct
4
Mode
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4
Clip
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4
alpha
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1
4
beta
0
1
4
bias
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0.2
4
derivTime
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0
4
s
intTime
0
20
4
s
gain
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2
4
gamma
0
1
4
tau
0
1
4
s
tauSet
0
1
4
s
MinInput
0
0
4
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0
1
4
MinOutput
0
0
4
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0
1
4
Input
0
0.700001
0
Output
0
0.600015
0
SetPoint
0
0.5
1
valve_flow
V1
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1103
792
0
79
51
pressure_changers/valve
V1
valve_flow
0
pressure_changers/valve
Inlet
Inlet
1
streams
Inlet
stream
1
NComp
0
2
0
F
0
1000
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
pressure_changers/valve
Outlet
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2
streams
Outlet
stream
2
NComp
0
2
0
F
0
1000
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
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z
0
0.499995
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1
0.500005
0
PP
0
PP
0
NComp
0
2
0
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0
4
kmol/h
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1000
4
kmol/h
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1
0
simple_sink
S1
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1258
667
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72
32
streams
S1
simple_sink
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streams
Inlet
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streams
Inlet
stream
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NComp
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F
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1000
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kmol/h
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329.986
0
K
P
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21.7033
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atm
h
0
-11778.5
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kJ/kmol
v
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0
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z
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0.499995
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0.500005
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heat_flow
H1
/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/heat_flow.png
913
688
0
80
66
controllers/heat_flow
H1
heat_flow
0
MinHeatFlow
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0
4
kW
MaxHeatFlow
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5000
4
kW
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2441.71
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kW
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0.488341
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valve_flow
V2
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1005
296
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79
51
pressure_changers/valve
V2
valve_flow
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pressure_changers/valve
Inlet
Inlet
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streams
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stream
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F
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600.015
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kmol/h
T
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300.001
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K
P
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10.8632
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atm
h
0
-15766.6
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kJ/kmol
v
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z
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0.500002
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0.499998
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pressure_changers/valve
Outlet
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streams
Outlet
stream
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F
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600.015
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kmol/h
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P
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10.8632
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atm
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-15766.6
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kJ/kmol
v
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PP
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kmol/h
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kmol/h
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0.600015
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simple_sink
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1295
352
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72
32
streams
S2
simple_sink
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streams
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streams
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kmol/h
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300.001
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K
P
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10.8632
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atm
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-15766.6
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kJ/kmol
v
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z
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0.500002
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Distillation_thermosyphon_cond
T1
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331
336.5
0
305.5
663.5
stage_separators/column
T1
Distillation_thermosyphon_cond
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stage_separators/column
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ColumnBasic
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stage_separators/column
INITIALIZATION
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stage_separators/column
INITIALIZATION
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0
TopTemperature
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328
4
K
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329
4
K
LevelFraction
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0.7
4
1
0.3
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0.01
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1
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stage_separators/column
CONTROL
CONTROL
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stage_separators/column
CONTROL
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Tindicator_TrayNumber
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stage_separators/column
TRAYS(1)
TRAYS
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stage_separators/tray
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tray
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stage_separators/tray
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trayBasic
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stage_separators/tray
InletLiquid
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streams
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stream
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F
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kmol/h
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328.462
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K
P
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atm
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-12041.5
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kJ/kmol
v
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z
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0.381538
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0.618462
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stage_separators/tray
InletVapour
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streams
InletVapour
stream
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F
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kmol/h
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328.615
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K
P
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20.0785
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atm
h
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-392.943
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kJ/kmol
v
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z
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stage_separators/tray
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streams
OutletLiquid
liquid_stream
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streams
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stream
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F
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kmol/h
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K
P
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atm
h
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-12049.1
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kJ/kmol
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z
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0.328462
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0.671538
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PP
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PP
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stage_separators/tray
OutletVapour
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2
streams
OutletVapour
vapour_stream
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streams
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stream
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F
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328.538
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K
P
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20.24
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atm
h
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-421.141
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kJ/kmol
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1
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z
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0.352974
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0.647026
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PP
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PP
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PP
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PP
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M
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0.643342
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1.22212
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ML
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0.616722
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kmol
MV
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1.24874
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kmol
E
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-10430.9
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kJ
vL
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9.91093e-05
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vV
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0.000917123
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0.038
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m
yideal
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0.352974
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0.647026
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rhoL
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438.244
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rhoV
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46.9779
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stage_separators/column
TRAYS(2)
TRAYS
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stage_separators/tray
TRAYS(2)
tray
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stage_separators/tray
TRAYS(2)
trayBasic
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stage_separators/tray
InletLiquid
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streams
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stream
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stage_separators/tray
InletVapour
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streams
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stream
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stage_separators/tray
OutletLiquid
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streams
OutletLiquid
liquid_stream
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streams
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stream
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PP
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stage_separators/tray
OutletVapour
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streams
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vapour_stream
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streams
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PP
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PP
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stage_separators/column
TRAYS(3)
TRAYS
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stage_separators/tray
TRAYS(3)
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trayBasic
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stage_separators/tray
InletLiquid
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streams
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stream
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stage_separators/tray
InletVapour
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stage_separators/tray
OutletLiquid
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streams
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liquid_stream
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stream
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PP
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OutletVapour
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vapour_stream
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streams
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PP
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stage_separators/column
TRAYS(4)
TRAYS
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stage_separators/tray
TRAYS(4)
tray
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TRAYS(4)
trayBasic
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InletLiquid
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streams
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stream
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stage_separators/tray
InletVapour
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streams
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stage_separators/tray
OutletLiquid
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streams
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liquid_stream
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stream
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PP
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OutletVapour
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vapour_stream
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PP
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stage_separators/column
TRAYS(5)
TRAYS
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stage_separators/tray
TRAYS(5)
tray
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TRAYS(5)
trayBasic
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streams
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stream
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stage_separators/tray
InletVapour
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stage_separators/tray
OutletLiquid
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streams
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liquid_stream
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stream
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PP
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stage_separators/tray
OutletVapour
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vapour_stream
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stage_separators/column
TRAYS(6)
TRAYS
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stage_separators/tray
TRAYS(6)
tray
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TRAYS(6)
trayBasic
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InletLiquid
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streams
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stream
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stage_separators/tray
InletVapour
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streams
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streams
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liquid_stream
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PP
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vapour_stream
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TRAYS(7)
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TRAYS(7)
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stream
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stage_separators/tray
InletVapour
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liquid_stream
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OutletVapour
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vapour_stream
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TRAYS(8)
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TRAYS(8)
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InletLiquid
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streams
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stream
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streams
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liquid_stream
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stream
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vapour_stream
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stage_separators/column
VapourDrawOff
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streams
VapourDrawOff
vapour_stream
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streams
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atm
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z
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PP
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stage_separators/column
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liquid_stream
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Reepmeyer
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327.996
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atm
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kJ/kmol
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liquid_stream
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stream
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0
kmol/h
T
0
300.001
0
K
P
0
10.8632
0
atm
h
0
-15766.6
0
kJ/kmol
v
0
0
0
z
0
0.500002
0
1
0.499998
0
PP
0
PP
0
stage_separators/condenser
OutletVapour
OutletVapour
2
streams
OutletVapour
vapour_stream
2
streams
OutletVapour
stream
2
NComp
0
2
0
F
0
0
1
kmol/h
T
0
300.001
0
K
P
0
10.8632
0
atm
h
0
-1343.62
0
kJ/kmol
v
0
1
0
z
0
0.53666
0
1
0.46334
0
PP
0
PP
0
PP
0
PP
0
NComp
0
2
0
V
0
2
4
m^3
Across
0
1
4
m^2
Kfactor
0
0.001
0
Levelpercent_Initial
0
0.7
0
Initial_Temperature
0
300
0
K
Initial_Composition
0
1
0
1
1
0
InletQ
0
1000
0
kW
TI
0
300.001
0
LI
0
0.700001
0
PI
0
10.8632
0
M
0
8.53809
0
kmol
1
8.51398
0
kmol
ML
0
16.7241
0
kmol
MV
0
0.327942
0
kmol
E
0
-266324
0
kJ
vL
0
8.37115e-05
0
m^3/mol
vV
0
0.00182959
0
m^3/mol
Level
0
1.4
0
m
Pdrop
0
1064.88
0
kPa
stage_separators/column
SPLITTER_TOP
SPLITTER_TOP
0
mixers_splitters/splitter
SPLITTER_TOP
splitter_column
0
mixers_splitters/splitter
Inlet
Inlet
1
streams
Inlet
stream
1
mixers_splitters/splitter
Reflux
Reflux
2
streams
Reflux
stream
2
mixers_splitters/splitter
Distillate
Distillate
2
streams
Distillate
stream
2
RefluxRatio
0
18
0
stage_separators/column
PUMP
PUMP
0
pressure_changers/pump
PUMP
pump
0
pressure_changers/pump
Inlet
Inlet
1
streams
Inlet
stream
1
NComp
0
2
0
F
0
257.149
0
kmol/h
T
0
300.001
0
K
P
0
10.8632
0
atm
h
0
-15766.6
0
kJ/kmol
v
0
0
0
z
0
0.500002
0
1
0.499998
0
pressure_changers/pump
Outlet
Outlet
2
streams
Outlet
streamPH
2
streams
Outlet
stream
2
NComp
0
2
0
F
0
257.149
0
kmol/h
T
0
300.006
0
K
P
0
11.0212
0
atm
h
0
-15766.6
0
kJ/kmol
v
0
0
0
z
0
0.500002
0
1
0.499998
0
PP
0
PP
0
PP
0
PP
0
NComp
0
2
0
dP
0
16
1
kPa
stage_separators/column
SUMP
SUMP
0
stage_separators/tank
SUMP
SumpTank
0
stage_separators/tank
InletLiquid
InletLiquid
1
streams
InletLiquid
stream
1
NComp
0
2
0
F
0
0.00173533
0
kmol/h
T
0
329.362
0
K
P
0
19.4351
0
atm
h
0
-12039.3
0
kJ/kmol
v
0
0
0
z
0
0.0136458
0
1
0.986354
0
stage_separators/tank
OutletLiquid
OutletLiquid
2
streams
OutletLiquid
liquid_stream
2
streams
OutletLiquid
stream
2
NComp
0
2
0
F
0
1828.94
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
PP
0
PP
0
stage_separators/tank
InletVapour
InletVapour
1
streams
InletVapour
stream
1
NComp
0
2
0
F
0
828.941
0
kmol/h
T
0
331.763
0
K
P
0
22.2362
0
atm
h
0
-1174.46
0
kJ/kmol
v
0
0.933945
0
z
0
0.499995
0
1
0.500005
0
stage_separators/tank
OutletVapour
OutletVapour
2
streams
OutletVapour
vapour_stream
2
streams
OutletVapour
stream
2
NComp
0
2
0
F
0
62718.4
0
kmol/h
T
0
329.986
0
K
P
0
21.5135
0
atm
h
0
-481.342
0
kJ/kmol
v
0
1
0
z
0
0.526446
0
1
0.473554
0
PP
0
PP
0
PP
0
PP
0
NComp
0
2
0
Heads
0
hemispherical
4
Diameter
0
1.6
4
m
Lenght
0
5
4
m
Levelpercent_Initial
0
0.7
0
Temperature_Initial
0
330
0
K
Composition_Initial
0
0.1
0
1
0.1
0
InletQ
0
0
1
kW
Vtotal
0
12.1978
0
m^3
Vfilled
0
8.53608
0
m^3
TotalHoldup
0
45.3065
0
kmol
1
45.08
0
kmol
LiquidHoldup
0
86.0882
0
kmol
VapourHoldup
0
4.29836
0
kmol
E
0
-1.04288e+06
0
kJ
vL
0
9.91551e-05
0
m^3/mol
vV
0
0.000851878
0
m^3/mol
Level
0
4.51216
0
m
Peq
0
21.5135
0
atm
Pstatic
0
0.189837
0
atm
LI
0
0.699807
0
TI
0
329.986
0
stage_separators/column
SPLITTER_BOTTOM
SPLITTER_BOTTOM
0
mixers_splitters/splitter
SPLITTER_BOTTOM
splitter2
0
mixers_splitters/splitter
Inlet
Inlet
1
streams
Inlet
stream
1
NComp
0
2
0
F
0
1828.94
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
mixers_splitters/splitter
Outlet1
Outlet1
2
streams
Outlet1
stream
2
NComp
0
2
0
F
0
1000
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
mixers_splitters/splitter
Outlet2
Outlet2
2
streams
Outlet2
stream
2
NComp
0
2
0
F
0
828.941
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
FlowRatios
0
0.546764
0
1
0.453236
0
stage_separators/column
REBOILER
REBOILER
0
stage_separators/reboiler
REBOILER
reboilerSteady
0
stage_separators/reboiler
InletLiquid
InletLiquid
1
streams
InletLiquid
stream
1
NComp
0
2
0
F
0
828.941
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
stage_separators/reboiler
OutletVapour
OutletVapour
2
streams
OutletVapour
streamPH
2
streams
OutletVapour
stream
2
NComp
0
2
0
F
0
828.941
0
kmol/h
T
0
331.763
0
K
P
0
22.2362
0
atm
h
0
-1174.46
0
kJ/kmol
v
0
0.933945
0
z
0
0.499995
0
1
0.500005
0
PP
0
PP
0
PP
0
PP
0
NComp
0
2
0
Pdrop
0
-54
4
kPa
FlowConstant
0
5
4
InletQ
0
2441.71
0
kW
vV
0
0.000817313
0
m^3/mol
rhoV
0
52.7195
0
kg/m^3
TI
0
331.763
0
PI
0
22.2362
0
stage_separators/column
FeedTray
FeedTray
1
streams
FeedTray
stream
1
NComp
0
2
0
F
0
700
0
kmol/h
T
0
323.15
0
K
P
0
20.4096
0
atm
h
0
-12826.4
0
kJ/kmol
v
0
0
0
z
0
0.4
0
1
0.6
0
stage_separators/column
VapourDistillate
VapourDistillate
2
streams
VapourDistillate
vapour_stream
2
streams
VapourDistillate
stream
2
NComp
0
2
0
F
0
0
0
kmol/h
T
0
300.001
0
K
P
0
10.8632
0
atm
h
0
-1343.62
0
kJ/kmol
v
0
1
0
z
0
0.53666
0
1
0.46334
0
PP
0
PP
0
stage_separators/column
LiquidDistillate
LiquidDistillate
2
streams
LiquidDistillate
liquid_stream
2
streams
LiquidDistillate
stream
2
NComp
0
2
0
F
0
600.015
0
kmol/h
T
0
300.001
0
K
P
0
10.8632
0
atm
h
0
-15766.6
0
kJ/kmol
v
0
0
0
z
0
0.500002
0
1
0.499998
0
PP
0
PP
0
stage_separators/column
BottomProduct
BottomProduct
2
streams
BottomProduct
liquid_stream
2
streams
BottomProduct
stream
2
NComp
0
2
0
F
0
1000
0
kmol/h
T
0
329.986
0
K
P
0
21.7033
0
atm
h
0
-11778.5
0
kJ/kmol
v
0
0
0
z
0
0.499995
0
1
0.500005
0
PP
0
PP
0
RefluxRatio
0
18
1
Q_cond
0
1000
0
kW
Q_reb
0
2441.71
0
kW
TI_cond
0
300.001
0
LI_cond
0
0.700001
0
PI_cond
0
10.8632
0
TI_reb
0
331.763
0
PI_reb
0
22.2362
0
LI_sump
0
0.699807
0
TI_sump
0
329.986
0
heat_flow
H2
/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/heat_flow.png
886
168
0
80
66
controllers/heat_flow
H2
heat_flow
0
MinHeatFlow
0
-1000
0
kW
MaxHeatFlow
0
1000
0
kW
HeatFlow
0
1000
0
kW
HeatFlowFraction
0
1
0
simple_sink2
S3
/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/Sink2.png
54
18
0
72
32
streams
S3
simple_sink2
0
streams
Inlet
Inlet
1
streams
Inlet
stream
1
NComp
0
2
0
F
0
0
0
kmol/h
T
0
300.001
0
K
P
0
10.8632
0
atm
h
0
-1343.62
0
kJ/kmol
v
0
1
0
z
0
0.53666
0
1
0.46334
0
PID
PIDT_condenser
/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/PID.png
944
34
0
62.5
58
controllers/PIDs
PIDT_condenser
PID
0
PID_Select
0
Ideal_AW
4
Action
0
Reverse
4
Mode
0
Automatic
4
Clip
0
Clipped
4
alpha
0
0.2
4
beta
0
1
4
bias
0
0.5
4
derivTime
0
10
4
s
intTime
0
100
4
s
gain
0
5
4
gamma
0
1
4
tau
0
1
4
s
tauSet
0
1
4
s
MinInput
0
250
4
MaxInput
0
380
4
MinOutput
0
0
4
MaxOutput
0
1
4
Input
0
300.001
0
Output
0
1
0
SetPoint
0
(273+45)
1
8
1182
829.562
1258
683.986
V1
Outlet
S1
Inlet
7
1142.75
521
1142.5
792
PIDL_sump
Output
V1
FlowFraction
10
1037.75
618
953
688
PIDT_reboiler
Output
H1
HeatFlowFraction
12
1084
333.562
1297
366
V2
Outlet
S2
Inlet
13
1258.75
134
1044.5
296
PIDL_Condenser
Output
V2
FlowFraction
1
200
291.768
331
701.425
feed
Outlet
T1
FeedTray
2
636.5
459.248
1005
333.562
T1
LiquidDistillate
V2
Inlet
3
349.33
1000
1105
830
T1
BottomProduct
V1
Inlet
4
913
727.6
636.5
973.46
H1
HeatFlow
T1
Q_reb
5
886
207.6
636.5
336.5
H2
HeatFlow
T1
Q_cond
6
126
34.9856
520.41
336.5
S3
Inlet
T1
VapourDistillate
9
636.5
946.92
1004
589
T1
TI_reb
PIDT_reboiler
Input
11
636.5
840.76
1113
491
T1
LI_sump
PIDL_sump
Input
14
636.5
392.234
1234
103
T1
LI_cond
PIDL_Condenser
Input
15
944
34
929
167
PIDT_condenser
Output
H2
HeatFlowFraction
16
477.64
336.5
948
61
T1
TI_cond
PIDT_condenser
Input