computational study of liquid-liquid dispersion in a rotating disc contactor a. vikhansky and m....

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Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of Cambridge, UK M. Simon, S. Schmidt, H.-J. Bart Department of Mechanical and Process Engineering, Technical University of Kaiserslautern, Germany

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Page 1: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor

A. Vikhansky and M. KraftDepartment of Chemical Engineering,

University of Cambridge, UK

M. Simon, S. Schmidt, H.-J. BartDepartment of Mechanical and Process Engineering,

Technical University ofKaiserslautern, Germany

Page 2: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Rotating disc contactor

Department of Mechanical and Process Engineering, Technical

University of Kaiserslautern,Kaiserslautern, Germany

cm 15

cQ

dQ

Page 3: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Flow patterns

Page 4: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

The approach

• Compartment model

• Weighted particles Monte Carlo method for population balance equations

• Monte Carlo method for sensitivity analysis of the Smoluchowski’s equations

• Parameters fitting

Page 5: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Compartment model:Breakage, coalescence,

transport

n t ,x;B n; D n;

t

Population balance equation

Page 6: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

0

00

( ) 1( ) ( ) ( )

2

( ) ( ) ( ) ; (0 ) ( ).

xn t xK x x x n t x x n t x dx

t

K x x n t x n t x dx n x n x

expH n t x H min

?

H

Smoluchowski's equation

Page 7: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Identification procedure

2. Assume a set of the model’s parameters.

3. Solve population balance equations.

4. Calculate the parametric derivatives of the solution.

5. Compare the solution with the experimental data and update the model’s parameters.

1. Formulate a model.

Page 8: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

11

( ) { ( ) ( )} ( ) ( ( )).N

N n nn

x t x t x t n t x w x x t

Stochastic particle system:

n

x

n

x

1

( )( ( )).

Nn

nn

wn t xx x t

A Monte Carlo method for sensitivity analysis of population balance equations

Page 9: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

11

( ) { ( ) ( )} ( ) ( ( )).N

N n nn

x t x t x t n t x w x x t

Stochastic particle system:

n

x

n

x

n

1

( )( ( )).

Nn

nn

wn t xx x t

A Monte Carlo method for sensitivity analysis of population balance equations

Page 10: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

0 0

( ) ( )( ) ( )

( )( ) ( ) ; (0 ) ( ) ( ).

m t x K x x xm t x x m t x dx

t xK x x

m t x m t x dx m x m x xn xx

( ) ( )m t x xn t x

A Monte Carlo method for sensitivity analysis of population balance equations

11

( ) ( )1;

{ ( ) }

Nk l l l

N

K x x w K x x w x

x K x x w x

11

( ) { ( ) ( )} ( ) ( ( )).N

N n nn

x t x t x t m t x w x x t

Stochastic particle system:

Page 11: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

1. generate an exponentially distributed time increment with parameter 1

ˆ ( ) ˆ1 N K x x w

x

2. choose a pair to collide according to the distribution

1

ˆ ( ) ˆˆ{ ( ) }ˆ

lk l lN

K x x xw

K x x xw

3. the coagulation is accepted with the probability

( )ˆ ( ) ˆ

k l l

lk l

K x x w

K x x w

4. or reject the coagulation and perform a fictitious jump that does not change the size of the colliding particles with the probability

( )1

ˆ ( ) ˆk l l

lk l

K x x w

K x x w

k k lx x x

ˆ ( ) ( )ˆ n nK x x K x x ww

Acceptance-rejection method

Page 12: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

1

1

( ) ( ) , ; ( ( ));

( ) (1 ) ( ( ));

N

n nn

N

n n nn

H t m h x m t x dx w h x t

H t m w W h x t

Calculation of parametric derivatives of the solution of the coagulation equation

1

( )( ( )).

N

n n nn

m t xw W x x t

A disturbed system:

1

( ) 1 ( ( ));

( ).

N

n n nn

m t x w W x x t

K x x

Page 13: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Evolution of the disturbed system is the same as the undisturbed one, while

the factors kW ln( )k k lW W K W

if the coagulation is accepted, or as ln( )

ˆˆl

k k l

l l

K WW W w K

w K w K

have to be recalculated as

if the coagulation is rejected

Page 14: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

2 2 31 1( ) ( )

2 2c cu D D 28.

The model: Breakage of the droplets

2 3

11 2

t /c

P D expD

D

D

Ds

6

2 1 3

2 3

1 /

/

u D

t D D

1/3

1 22/3 2/3 5/3exp

c

c cD D

Page 15: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

The model: Collision and coalescence

1 3 1 22 2 2 3 2 3

1 2 1 2 1 2 3 1 2 12 24 1

/ // /,h D D u u c D D D D

2

1 21,2 4 32

1 2

exp1c c D D

cD D

1,2 1,2 1,2K h

Page 16: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

The model: Transport

c

resrise

h

v D

1c

rise v T c v T

Qv D k v D v k v D

A

2/3 1/3

14.2 6

c d cT

c c

D Eëv D g

5Vk c

Page 17: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Operational conditions

Page 18: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Identified parameters and residuals

Page 19: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Experimental vs. numerical

results

fitted unfitted

Page 20: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Coefficients of sensitivity

ln

ln ic

Volume fraction

Mass-mean diameter

Sauter mean diameter

Page 21: Computational Study of Liquid-Liquid Dispersion in a Rotating Disc Contactor A. Vikhansky and M. Kraft Department of Chemical Engineering, University of

Conclusions

• A Monte Carlo method was applied to a population balance of droplets in two-phase liquid-liquid flow.

• The unknown empirical parameters of the model have been extracted from the experimental data.

• The coefficients identified on the basis of one set of experimental data can be used to predict the behaviour of the system under another set of operating conditions.

• The proposed method provides information about the sensitivity of the solution to the parameters of the model.