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24–28 April 2017, Vienna, Austria
A New Approach to Teach How to Analyze Tracing Results by a Rapid Visual Method
Olivier POTIER
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria2
Personal interests
2
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria3
Chemicaland processengineering
Watertreatment
Internationalrelationship
Innovativedesign
Innovation
Personal interests
2
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria4
HydrodynamicsmodelingTracing
Reactormodeling
Compartmentalmodeling
River
Micropollutants
Personal interests
Chemicaland processengineering
Watertreatment
Internationalrelationship
Innovativedesign
Innovation
2
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria5
HydrodynamicsmodelingTracing
Reactormodeling
Compartmentalmodeling
River
Micropollutants
this talk
Personal interests
Chemicaland processengineering
Watertreatment
Internationalrelationship
Innovativedesign
Innovation
2
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria6
Residence Time Distribution
3
Inlet
signalOutlet
signal
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria7
Residence Time Distribution
3
t
E(t)C(t)
t
00
1
N
)t(C.Q
dt
dN.
N)t(E
1
3
3
.. molm
mol
s
m1s
0
).(
)()(
dttC
tCtE
dttCQdN ).(.
sm
mol
s
m..
3
3
mol
00
0 ).().(. dttCQdttCQN
Inlet
sign
al
Outlet
signalPulse injection
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria8
Simple reactor models
4
CSTR(Continuous Stirred (Flow) Tank Reactor, Backmix Reactor,Mixed (Flow) Reactor,Gradientless Reactor)
Plug flow reactor
0 = ¶ uC( )¶z
æ
ææ
æ
ææ+
¶C
¶t
æ
ææ
æ
ææ
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria9
5
reactor in series
recycling
parallel
exchange
short-circuit
Systems are often more complex
How to represent them?
Use of virtual reactors to mimic the global hydrodynamics.
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria10
Systems are often more complex
6
CSTR(Continuous Stirred (Flow) Tank Reactor,
Backmix Reactor,Mixed (Flow) Reactor,Gradientless Reactor)
Plug flow reactor
Plug flow reactor with axial dispersion0 =
¶ uC( )¶z
æ
ææ
æ
ææ - D
¶2C
¶z2 +
¶C
¶t
æ
ææ
æ
ææ
Cascade of CSTRs
0 = ¶ uC( )¶z
æ
ææ
æ
ææ+
¶C
¶t
æ
ææ
æ
ææ
Q Q
J CSTRs
Pe= uL
DPeclet Number
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria11
Effect of flowrate change
7
Wastewater
Recycled sludge
REACTOR
settler
Example of the channel reactor:volume 3300 m3, total length 102 m
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria12
Effect of flowrate change
7
Wastewater
Recycled sludge
REACTOR
settler
Example of the channel reactor:volume 3300 m3, total length 102 m
0
5
10
15
20
25
30
40 90 140 190 240 290 340
J
t (min)
J (full scale plant)
J (pilot plant) 0
5
10
15
20
25
30
35
40
0,00 0,01 0,01 0,02 0,021/ t (min
-1)
Pe
STEP
pilote
t.
. 2
D
L
D
LuP
Water Research, Potier et al., 2005
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria13
Effect of flowrate, shape and size
7
Wastewater
Recycled sludge
REACTOR
settler
0
5
10
15
20
25
30
40 90 140 190 240 290 340
J
t (min)
J (full scale plant)
J (pilot plant) 0
5
10
15
20
25
30
35
40
0,00 0,01 0,01 0,02 0,021/ t (min
-1)
Pe
STEP
pilote
t.
. 2
D
L
D
LuP
Water Research, Potier et al., 2005
l
wl.w.Q
wh
hD aerationG
23
2
Water Research, Le Moullec et al., 2008
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria14
How to identify the kind of virtual reactors association?
8
Looking at the RTD graph, people need to be able to rapidly identify the kind of complex virtual reactors association in the system,
and so, need to understand:- the effect of parallel reactors association- the effect of the arrangement of reactors in series- that different associations can lead to similar RTD- the effect of recirculation
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria15
8
Looking at the RTD graph, people need to be able to rapidly identify the kind of complex virtual reactors association in the system,
and so, need to understand:- the effect of parallel reactors association- the effect of the arrangement of reactors in series- that different associations can lead to similar RTD- the effect of recirculation
TRAINING METHOD: we propose to use the software DTS in an unusual way to perform simulation of different kind of associations.
How to identify the kind of virtual reactors association?
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria16
TRAINING METHOD: CSTR
9
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria17
TRAINING METHOD: reactors in series
10
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria18
TRAINING METHOD: reactors in series
10
Series (CSTR + PFR)
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria19
TRAINING METHOD: reactors in series
10
Series (CSTR + PFR)
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria20
TRAINING METHOD: reactors in series
10
Series (CSTR + PFR)
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria21
TRAINING METHOD: Series or Parallel
11
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria22
TRAINING METHOD: Series or Parallel
11
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria23
TRAINING METHOD: Series or Parallel
11
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria24
TRAINING METHOD: Series or Parallel
11
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria25
TRAINING METHOD
12
CascadeOf CSTR
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria26
TRAINING METHOD
12
CascadeOf CSTR
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria27
TRAINING METHOD
12
CascadeOf CSTR
CascadeOf CSTR
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria28
TRAINING METHOD
12
CascadeOf CSTR
CascadeOf CSTR
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria29
TRAINING METHOD
12
CascadeOf CSTR
CascadeOf CSTR
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria30
TRAINING METHOD: Parallel Cascades
13
MeasureCascade
of 2 CSTRs
Cascadeof 6 CSTRs
Cascadeof 20 CSTRs
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria31
TRAINING METHOD: Parallel Cascades
13
MeasureCascade
of 2 CSTRs
Cascadeof 6 CSTRs
Cascadeof 20 CSTRs
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria32
TRAINING METHOD: Parallel Cascades
13
MeasureCascade
of 2 CSTRs
Cascadeof 6 CSTRs
Cascadeof 20 CSTRs
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria33
TRAINING METHOD: cascades with recirculation
14
Cascade of15 CSTRs
Cascade of15 CSTRs
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria34
TRAINING METHOD: cascades with recirculation
14
Cascade of15 CSTRs
Cascade of15 CSTRs
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria35
TRAINING METHOD: Stegosaurus RTD?
15
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria36
TRAINING METHOD: Stegosaurus RTD?
15
Thank you for your attention.
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria39
Chemical Reaction Engineering
4
Plug Flow Reactor: CSTR:
Example with a chemical reaction:
• Q=10 m3/h of a reactant solution
•Conversion Yield : 99 %
• A P
• First order kinetics (k = 4 h-1)
-rA = kCA = rP
Génie de la réaction chimique, Jacques Villermaux, Edition Tec&Doc Lavoisier
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria40
Chemical Reaction Engineering
4
Volume of the Plug Flow Reactor:VPFR = t Q = 11,5 m3
Plug Flow Reactor:
h 151 990 1
1
4
1
X1
1
k
1 ,
,lnln
t
CSTR:
h 24,75
0,99 1
0,99
4
1
X1
X
k
1
t
Volume of the CSTR:VCSTR = t Q = 248 m3
Example with a chemical reaction:
• Q=10 m3/h of a reactant solution
•Conversion Yield : 99 %
• A P
• First order kinetics (k = 4 h-1)
-rA = kCA = rP
Génie de la réaction chimique, Jacques Villermaux, Edition Tec&Doc Lavoisier
Olivier Potier, ICARST 2017, 24–28 April 2017, Vienna, Austria41
Chemical Reaction Engineering
4
CSTR
PFR
Volume of the Plug Flow Reactor:VPFR = t Q = 11,5 m3
Plug Flow Reactor:
h 151 990 1
1
4
1
X1
1
k
1 ,
,lnln
t
CSTR:
h 24,75
0,99 1
0,99
4
1
X1
X
k
1
t
Volume of the CSTR:VCSTR = t Q = 248 m3
22V
V
PFR
CSTR
Example with a chemical reaction:
• Q=10 m3/h of a reactant solution
•Conversion Yield : 99 %
• A P
• First order kinetics (k = 4 h-1)
-rA = kCA = rP
Génie de la réaction chimique, Jacques Villermaux, Edition Tec&Doc Lavoisier