Stabilization of a diluted H2 lifted jet flame:

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Stabilization of a diluted H2 lifted jet flame: numerical study and control

Christophe Duwig* - Haldor Topsøe A/S – DK-2800 Lyngby

*also with Dept. Energy Sciences – Lund University (Sweden)

Presentation layout

Background: reforming within ammonia technology

Presentation of the idealized problem & methodology

– Cabra’s jet flame

– Reactive LES simulation tool with tabulated chemistry

Presentation of the results

– comparisons with experimental data

– Analysis of vortex dynamics: identification of the coherent structures

– Effect of small perturbations upon these structures: vortex control

Conclusion

Overview of a Topsøe ammonia plant http://www.topsoe.com/Business_areas/Ammonia/Processes.aspx

(1) CH

4

+H

2

O=CO+6H

2

(2) CH

4

+0.5O

2

=>CO+2H

2

Flame!

CO+H

2

O=CO

2

+H

2

3H

2

+N

2

=>2NH

3

In real life, it looks like …

Burner/ flame location

CH

4

+H

2

O=CO+6H

2

CH

4

+0.5O

2

=>CO+2H

2

Secondary reformer burner

Process gas is a hot syngas: mixture CO, CO2, H20, H2, CH4

=

We deal with a hot but very diluted fuel

Process gas

Process gas air http://www.topsoe.com/Business_areas/Ammonia/Processes.aspx

Air nozzles: high-speed jets

How does a flame front really look like?

what we see and what we hear

Even simple a Bunsen flame is complex as shown beside!

There is a need of advanced investigation techniques (experimental and numerical), here laser based OH-PLIF

Does it happen only in the lab. ??? … NO!

OH PLIF from Buschmann et al., 26th Symp.

On Combustion, pp. 437-445, 1996

Emulation of a secondary reformer flame

Diluted H

2

/N

2

/O

2 flame in a hot coflow

X

X

IG http://www.me.berkeley.edu/cal/VCB/Data/

T~1045 K

H

2

O/O

2

/N

2

T~1045 K

H

2

O/O

2

/N

2

T~305 K

H

2

/N

2

Idealized scenario of a fuel fluid parcel:

The parcel:

Exits the nozzle

Is convected downtream

Mixes with vitiated gases - dilution

T , Z and Y

F

WITHOUT reaction Y

OH

~0

Mixes with vitiated gases and auto-ignites: reaction starts after a delay t~X

IG

/U

BULK

>

AI

(Z,T)

Burns and mixes further

Generation of kinetic lookup tables

X

System of equations: dY i i dt dT i

T dt

Initial conditions:

( t 0 )

Y

1

...

Y i

...

Y n

T

Z X

Fuel

•Two reaction coordintates

( , t) including detailed chemical kinetics

•PSR computations performed using Cantera

1 Z X

Ox

•Allow to store the chemical information in look-up talbes & mapping in the (Z, T)-space

Tabulated chemistry or Z or Z

Constitutive equations for reactive LES

Filtered continuity and Navier-Stokes u 0

SGS term: here FSF t u u u p u u uu u t

2 additional scalars: mixture fraction and temperature

~

Z u

~

Z (( D D

~

Z ).

t

~

T t u T

~

( D

T

D

~

T ) w

T

( Z , T )

Filtered density function: top-hat w

T

( Z , T ) w

T tabulation

( Z , T ) P (

~

Z , T

~

, Z , T ,...) dZdT

Numerical methods for reactive LES

• Numerical methods

• Finite Difference Cartesian code

• Spatial discretization: 4th order centred except the convective terms in the T & Z-eq. ->WENO5

• Temporal discretization: 2nd order implicit with multi-grid acceleration & CFL < 0.3

•Numerical grid

• Computational box: 22 d ·11 d ·11 d

• average cell size at the inlet h=d/20

• number of cells: 2 millions

•Vortices are visualized like

2

-isosurfaces (gray)

Mean quantities – comparisons with exp.

OH mass fraction & temperature

Direct light visualization

OH-field

Temperature [K]

Animation of the OH and temperature fields

T [K]

OH

Fuel jet

3D snapshot: flame & vortex dynamics

Jet core

Small vortex tubes

Flame envelope

Vortex rings

Vortex rings merge giving helices

Macro-mixing micro-mixing

Sequence: rings ->helices->small tubes->flame

Control by inflow perturbations A(t, ) u

JET

( X , t ) A ( t , ) u

Average

( X )

Fluctuation (Klein et al., JCP 2005) u ' ( X ) F ( t )

Promote Case base

A(t, )

1

Axi-sym.

1+0.05 2cos(2 ·St p

·t/

VariFlap 1+0.05 2cos(2 ·St p

·t/ +

0.05 2cos( ·St p

·t/ ·(2y/d)

Star 1+0.2 cos(5 ) · (2r/d) rings helices

Small scale vortex tubes

Coflow

Jet daSilva & Métais, PoF, 2002

Axisymmetric pulsation:

3D vortices and 2D OH field

Vortex ring

Tubes

Flame leading edges

VariFlap perturbation:

3D vortices and 2D temperature field

Sequence from daSilva & Métais, PoF 2002

VafiFlap perturbation:

3D vortices and 2D OH field

Star:

3D vortices and temperature field

Star:

3D vortices and OH field

Conclusion and prospects

Turbulent combustion is still a fascinating and mysterious thing

A small amplitude perturbation enables to control the flame dynamics (jet core length, leading edge position, …)

The star perturbation attaches the flame -> dramatic reduction of the flame fluctuation -> attractive stabilization tool!!

– Already used for noise reduction

Chevron on nozzles for jet noise reduction

Callender et al. AIAA J., 2005

Modeling: ideal PSR interpretation

Vitiated gas

Fuel mixture

( ,t) are the reaction coordinates t( )

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