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   Machine Learning Based Filtered Drag Force Model    Machine Learning Based Filtered Drag Force Model

  Machine Learning Based Filtered Drag Force Model - PowerPoint Presentation

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  Machine Learning Based Filtered Drag Force Model - PPT Presentation

Yundi Jiang Jari Kolehmainen Yile Gu Yannis Kevrekidis Ali Ozel amp Sankaran Sundaresan Princeton University NJ  2018 NETL Workshop on Multiphase Flow Science 1 ID: 805252

drift grid coarse simulation grid drift simulation coarse model velocity filtered drag scale particle fine gas euler test coefficient

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Slide1

  Machine Learning Based Filtered Drag Force ModelYundi Jiang, Jari Kolehmainen, Yile Gu Yannis Kevrekidis , Ali Ozel & Sankaran SundaresanPrinceton University, NJ  2018 NETL Workshop on Multiphase Flow Science

1

Funded

by ExxonMobil

Slide2

Gas–particle flows in fluidized bedsInherently unstable with multiscale structuresWeight of particle is principally balanced by the drag forceAccurate estimation of the drag force is essential for reliable prediction of flow behaviorBackground 2 Frank Schaffer, NETL

Slide3

Fine-grid simulations1Euler-Euler ApproachContinuum averaged equations of motion for the fluid and solid phasesCoarse-grid simulationsFiltered Euler-Euler ApproachMulti-scale structures in gas-particle Flow1. Igci, Y., Andrews, A. T., Sundaresan

, S., Pannala, S. and O'Brien, T. (2008), Filtered two-fluid models for fluidized gas-particle suspensions. AIChE

J., 54:

1431–1448

3

Slide4

 

Particle phase momentum balance in

Filtered Two-fluid

model

Multi-scale structures in

gas-particle

Flow

4

Upon filtering

=

 

Particle phase

momentum balance in

Two-fluid model

Slide5

5Sub-grid scale terms:Sub-grid scale contribution to drag force

Meso

-

scale stress:

S

ub-grid scale contribution to gas-phase stress:

Sub-grid scale contribution to

solid-phase stress (Kinetic Theory):

 

Multi-scale structures in gas-particle Flow

- unresolved

structures in filtered models

- need

to be modeled to account for

meso

-scale

inhomogeneities

 

most significant

5

.

Parmentier

, J.-F.,

Simonin

, O. and

Delsart

, O

.,

(2012),

AIChE

J., 58: 1084–1098

6

.

Ozel

,

A.,

Fede

,

P.,

Simonin

,

O., (

2013)

Int. J

Multiph

.

Flow,

55:43-63 0301 -93222.

7

.

Ozel

, A. et al., (2017)

Physics of Fluid

(2017) 29: 103308.

Slide6

Prior studies from our group Drag correction

 

Modeling filtered drag force

6

3

.

Igci

, Y.,

Sundaresan

, S.,

(

2011)

 

Ind. Eng. Chem.

Res.

50

 (23

): 13190-13201

4

. Milioli,C., Milioli, F.E., Holloway, W., Kapil, A., Sundaresan, S., (2013). AIChE J. 59..

Slide7

: Microscopic drag coefficient evaluated with filtered variables

: Drift velocity

 

Modeling filtered drag force

7

Toulouse group approach

5,6

and also our current

approach

7

Takes into account

inhomogeneities

inside filtering volume

Difference between filtered gas velocity and gas velocity seen by the particles

Not available in coarse simulations - need to be modeled

5

.

Parmentier

, J.-F., Simonin, O. and Delsart, O., (2012), AIChE J., 58: 1084–10986. Ozel, A.,Fede, P., Simonin, O., (2013) Int. J Multiph. Flow, 55:43-63 0301 -93222.7. Ozel, A. et al., (2017) Physics of Fluid (2017) 29: 103308.

Slide8

Drag correction needs drift velocityChallenge: drift velocity is NOT available in a filtered model simulation. It needs to be estimated5-7Scale similarity approach Good a priori resultPearson correlation coefficient : 0.8 for with

( for smaller filter size)

Good agreement between fine and coarse simulation results

Approach

in the current study

Derive a transport equation for drift velocity

Analyze the transport equation to identify key quantities

Use data mining approach to obtain closure model

 

Drift velocity for drag force correction

8

7.

Ozel

, A. et al., (2017) Physics of Fluid (2017) 29: 103308.

Slide9

9Flow Configuration & Simulation ParametersFine-grid Euler-Euler simulationParticle diameter

75

Grid size (

) : 3

x 3 x 3

Particle

density [

: 1500

Restitution coefficient: 0.9

Gas density [

: 1.3

Gas viscosity [

]:

 

Slide10

Filtering Euler-Euler resultsCollect fine-grid simulation resultsFilter all relevant quantities using a filter of chosen sizeFiltered variables:

Sub-grid scale terms

Budget Analysis

Additional quantities: Filtered drag, drift velocity, etc.

 

Fine-grid Euler-Euler simulation

10

 

Slide11

Derivation

Sub-grid scale correlations on the right hand side: 13!

 

Transport equation for drift

v

elocity

11

Slide12

Budget Analysis: Assess relative magnitudes of the terms

 

12

Transpor

t equation for drift

v

elocity

Potential markers for predicting

 

Slide13

Can handle big dataGreat predictive capabilityDatasetInput: Local filtered variables (filter size

) and their gradientsOutput: axial directional drift flux:

Model:

 

Constitutive models with machine

l

earning

13

Neural Network

model for

predicting drift velocity

Slide14

14A priori test for predicting : Pearson Correlation Coefficient for Neural Network Model: 0.99

Significant improvement from model without

Pearson correlation coefficient

for two marker

(

) scale similarity

model approach was 0.8

6

 

A priori Test: Neural Network Model

Probability Density

Error percent

Predicted

 

Real

 

6.

Ozel

, A.,

Fede

, P., Simonin, O., (2013) Int. J Multiph. Flow, 55:43-63 0301 -93222. is an important marker for predicting drift velocity 

Slide15

Grid size is 9X of the fine-grid simulation : Grid size (

) = 27 x 27 x 27

Same

flow

configuration

Coarse drag coefficient corrected by drift velocity

 

15

Model validated by coarse Euler-Euler simulation

A p

osteriori

Test: Coarse-grid Simulation

From a priori study:

Pearson

Correlation Coefficient =

0.99

 

NN Model

 

 

 

 

7.

Ozel

, A. et al., (2017)

Physics of Fluid

(2017) 29: 103308.

Slide16

16Simulation SnapshotsA posteriori Test: Coarse-grid Simulation

 

(a)

Fine-grid (3

d

p

)

(b)

Fine-grid (3

d

p

) result mapped on coarse grid (27

d

p

)

(c)

Coarse-grid (27

d

p) with

vd corrected Wen&Yu

(d)Coarse-grid (27 dp) with Wen&Yu

Slide17

17Axial Direction Solid Volume Fraction Profile A posteriori Test: Coarse-grid SimulationDimension HeightWen&Yu overpredicts

the bed height for coarse-grid simulation

Drift velocity correction effectively correct drag coefficient - bring the bed expansion closer to fine-grid results

27

3

27

Slide18

18A posteriori Test: Coarse-grid Simulation(a) Wen&Yu. (b) Wen&Yu +

v

d

Particle volume fraction vs. bed elevation

Slide19

19Horizontal Direction Solid flux profileA posteriori Test: Coarse-grid SimulationMean Solid flux =

, averaged over y-axis for certain horizontal layer

 

Z= 40% Bed

Height

Z= 80% Bed

Height

Wen&Yu

underpredicts

solid flux across the bed and

overpredicts

the bed expansion

Drift

velocity correction produces similar profile as fine-grid simulation

27

27

27

27

Dimensionless Horizontal

Position

Dimensionless Horizontal PositionDimensionless Solid FLuxDimensionless Solid FLux

Slide20

20Axial Direction Drift Flux Profile Drift flux = Inside bedCoarse-grid Fine-gridTop and Bottom of bedCoarse-grid simulation results

overpredict the magnitude of drift fluxModel performance is affected by sharp gradients

model improvement is needed

 

A posteriori

Test: Coarse-grid Simulation

27

Dimensionless

Drift

FLux

Dimensionless

Height

Slide21

Drift velocity is an essential marker for filtered drag coefficient correctionA transport equation for drift velocity is derived and simplified to identify proper markers for modeling drift velocityNeural Network model is developed for drift velocity based on filtered fine-grid simulation resultsNeural Network model is validated with coarse-grid simulation; Posteriori test results show agreement between coarse and filtered fine-grid simulation resultsFuture work: Explicit model form Other gas-particle systems Heat and mass transport in gas-particle flowSummary

21