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'''Application Challenge AC2-09'''   © copyright ERCOFTAC {{CURRENTYEAR}}  
'''Application Challenge AC2-09'''   © copyright ERCOFTAC {{CURRENTYEAR}}  
==Introduction==  
==Introduction==  
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Sandia flame D [1] (shown in Fig.1) is a widely used  test  case  for
validation of numerical models of  non-premixed  combustion.  The  fuel
stream is composed of 25% methane (CH4) and 75% air. The pilot flame is
a lean mixture of C2H2, H2, air, CO2  and  N2  with  the  same  nominal
enthalpy and equilibrium as methane/air at the equivalence ratio  0.77.
Partial premixing with air also reduces the flame length and produces a
more robust flame than pure CH4 or nitrogen-diluted CH4.  Consequently,
the flames may be operated at  reasonably  high  Reynolds  number  with
little or no local extinction, even with a  modest  pilot.  The  mixing
rates are high enough that these flames burn as diffusion flames,  with
a single reaction zone near the stoichiometric mixture fraction and  no
indication of significant premixed reaction in  the  fuel-rich  CH4/air
mixtures. Flame D (Re=22400) has a small degree of local extinction. It
can be assumed that the Flame D operates  in  a  flamelet  regime  that
means there is a scale separation between turbulence  length  and  time
scales and the scales characterizing the  combustion  process.  Despite
that the Sandia D Flame is not a demanding test case  it  seems  to  be
worth to study various combustion/turbulence interaction models on this
example as a starting point to more complex flame with local extinction
and reignition.  As an Application Challenge such a  flame  facilitates
to  study  models  of  turbulence/chemistry  interaction  allowing  to
separate  the  influence  of  turbulence  and  turbulence/chemistry
interaction models from the influence of chemical kinetics applied.
 
Focusing on the LES approach to the Sandia Flame D, one of the  first
3D-LES of this flame type was presented by di Mare and  Jones  in  1999
[2] who  applied  simple  steady  flamelet  model.  Then  a  simplified
Conditional Moment  Closure  (CMC)  with  the  Conditional  Source-term
Estimation (CSE) proposed by Steiner and Bushe [3] was tested  also  on
Sandia D. Very convincing results using  unsteady-flamelet  model  were
obtained by Pitsch and  Steiner  [4].  More  recently  the  Conditional
Moment  Closure  equations  in  the  context  of  LES  filtration  were
formulated by Navarro-Martinez et al. [5] and  full  CMC  approach  was
validated using Sandia D flame. The LES-CMC approach was  also  applied
by Garmory and Mastorakos [6] for Sandia D and F  Flames.  The  results
were very good for Sandia D Flame, however,  application  of  the  same
settings to Sandia F Flame resulted in underprediction of the extent of
local extinction. The LES with steady flamelet for Sandia  D  was  also
exploited by Kempf et al. [7] to study the  structure  of  a  diffusion
flame  in  terms  of  length  scales,  scalar  dissipation  and  flame
orientation. A new premixed flamelet approach based on  two  additional
equations for the mixture fraction and for the  progress  variable  was
proposed by Vreman et al. [8]. This in principle universal concept  was
validated on both premixed  preheated  Bunsen  flame  and  non-premixed
Sandia Flame D. The flamelet/progress variable model was  also  applied
by Ihme and Pitsch [9,10] and used to predict extinction and reignition
in Sandia Flames D and E.  The concept of Steiner and Bushe [3] of  the
Conditional Source-term Estimation (CSE) was again applied by  Ferraris
and Wen [11] with some modifications reducing the number  of  flamelets
and  again  validated  on  Sandia  D.  The  models  based  on  LES  and
transported PDF/FDF approach were also applied and validated using this
flame. One of the first woks of this type was proposed by  Sheikhi  et.
al. [12]. Bisetti and Chen [13] tested various mixing models using  LES
and Eulerian PDF method. Jones and Prasad  [14] performed  calculations
for Sandia Flame D,E and F with LES and the Eulerian  stochastic  field
method showing ability of the model to reproduce local  extinction  and
reignition
 
Within the current Application Challenge attention is focused on the
LES calculation  only  and  neither  RANS  nor  URans  predictions  are
analyzed.
 
==Relevance to Industrial Sector==  
==Relevance to Industrial Sector==  
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<!--{{Demo_AC_Desc_Relev}}-->

Revision as of 08:11, 28 April 2011


Front Page

Description

Test Data

CFD Simulations

Evaluation

Best Practice Advice

SANDIA Flame D

Application Challenge AC2-09   © copyright ERCOFTAC 2024

Introduction

Sandia flame D [1] (shown in Fig.1) is a widely used test case for validation of numerical models of non-premixed combustion. The fuel stream is composed of 25% methane (CH4) and 75% air. The pilot flame is a lean mixture of C2H2, H2, air, CO2 and N2 with the same nominal enthalpy and equilibrium as methane/air at the equivalence ratio 0.77. Partial premixing with air also reduces the flame length and produces a more robust flame than pure CH4 or nitrogen-diluted CH4. Consequently, the flames may be operated at reasonably high Reynolds number with little or no local extinction, even with a modest pilot. The mixing rates are high enough that these flames burn as diffusion flames, with a single reaction zone near the stoichiometric mixture fraction and no indication of significant premixed reaction in the fuel-rich CH4/air mixtures. Flame D (Re=22400) has a small degree of local extinction. It can be assumed that the Flame D operates in a flamelet regime that means there is a scale separation between turbulence length and time scales and the scales characterizing the combustion process. Despite that the Sandia D Flame is not a demanding test case it seems to be worth to study various combustion/turbulence interaction models on this example as a starting point to more complex flame with local extinction and reignition. As an Application Challenge such a flame facilitates to study models of turbulence/chemistry interaction allowing to separate the influence of turbulence and turbulence/chemistry interaction models from the influence of chemical kinetics applied.

Focusing on the LES approach to the Sandia Flame D, one of the first 3D-LES of this flame type was presented by di Mare and Jones in 1999 [2] who applied simple steady flamelet model. Then a simplified Conditional Moment Closure (CMC) with the Conditional Source-term Estimation (CSE) proposed by Steiner and Bushe [3] was tested also on Sandia D. Very convincing results using unsteady-flamelet model were obtained by Pitsch and Steiner [4]. More recently the Conditional Moment Closure equations in the context of LES filtration were formulated by Navarro-Martinez et al. [5] and full CMC approach was validated using Sandia D flame. The LES-CMC approach was also applied by Garmory and Mastorakos [6] for Sandia D and F Flames. The results were very good for Sandia D Flame, however, application of the same settings to Sandia F Flame resulted in underprediction of the extent of local extinction. The LES with steady flamelet for Sandia D was also exploited by Kempf et al. [7] to study the structure of a diffusion flame in terms of length scales, scalar dissipation and flame orientation. A new premixed flamelet approach based on two additional equations for the mixture fraction and for the progress variable was proposed by Vreman et al. [8]. This in principle universal concept was validated on both premixed preheated Bunsen flame and non-premixed Sandia Flame D. The flamelet/progress variable model was also applied by Ihme and Pitsch [9,10] and used to predict extinction and reignition in Sandia Flames D and E. The concept of Steiner and Bushe [3] of the Conditional Source-term Estimation (CSE) was again applied by Ferraris and Wen [11] with some modifications reducing the number of flamelets and again validated on Sandia D. The models based on LES and transported PDF/FDF approach were also applied and validated using this flame. One of the first woks of this type was proposed by Sheikhi et. al. [12]. Bisetti and Chen [13] tested various mixing models using LES and Eulerian PDF method. Jones and Prasad [14] performed calculations for Sandia Flame D,E and F with LES and the Eulerian stochastic field method showing ability of the model to reproduce local extinction and reignition

Within the current Application Challenge attention is focused on the LES calculation only and neither RANS nor URans predictions are analyzed.

Relevance to Industrial Sector

Design or Assessment Parameters

Flow Domain Geometry

Flow Physics and Fluid Dynamics Data




Contributed by: Andrzej Boguslawski — Technical University of Częstochowa

Front Page

Description

Test Data

CFD Simulations

Evaluation

Best Practice Advice


© copyright ERCOFTAC 2024