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7/28/2019 Lecture12_2012
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Lecture 12
The Level Set Approach for Turbulent PremixedCombus=on
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A model for premixed turbulent combus7on, based on the non-reac7ng scalar Grather than on progress variable, has been developed in recent years
It avoids complica7ons associated with counter-gradient diffusion and, since Gis non-reac7ng, there is no need for a source term closure
An equa7on for G can be derived
by considering an iso-scalar surface
This surface divides the ow eld intotwo regions where
G > G0 is the region of burnt gas
andG < G0 is that of the unburnt mixture
The choice of G0 is arbitrary and typically taken as G0 = 0
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Recapitula=on Flame front normal vector in direc7on of the unburnt gas
Flame displacement speed d x f /dt
A eld equa7on can now be derivedby differen7a7ng
with respect to 7me
This leads to
12.-3
DG
Dt= 0
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Introducing
and
one obtains the eld equa7on
This equa7on was introduced byWilliams (1985)
It is known as the G-equa7on
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G-equa7on is applicable to thin ame structures propaga7ng with a well-dened burning velocity
It therefore is well-suited for the descrip7on of premixed turbulentcombus7on in the corrugated amelets regime, where it is assumed that
the laminar ame thickness is smaller than the smallest turbulent length
scale, the Kolmogorov scale
Therefore, the en7re ame structure is embedded within a locally quasi-
laminar ow eld and the laminar burning velocity remains well-dened
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The G-equa7on
has no diffusion term
G is a scalar quan7ty which is dened at the ame surface only , while thesurrounding G-eld is not yet uniquely dened
This originates from the fact that the kinema7c balance
is valid only for the ame surface and deni7on of remaining G-eld is (within
some constraints) arbitrary
G-eld typically dened to be the closest distance from the ame
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The burning velocity sL appearing in
may be modied to account for the effect of ame stretch
Performing two-scale asympto7c analyses of corrugated premixed ames,Pelce and Clavin (1982), Matalon and Matkowsky (1982) derived rst order
correc7on terms for small curvature and strain
Expression for the modied burning velocity becomes
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The expression for the modied burning velocity becomes
Here sL0 is the burning velocity of the unstretched ame, is the curvatureand S is the strain rate
Flame curvature is dened in terms of the G-eld as
where
has been used Flame curvature is posi7ve if ame is convex with respect to unburnt mixture
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The strain rate imposed on the ame by velocity gradients is dened as
The Markstein length is of the same order of magnitude and propor7onalto the laminar ame thickness
The ra7o is called the Markstein number
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For the case of a one-step reac7on with a large ac7va7on energy , constanttransport proper7es and a constant heat capacity, the Markstein length with
respect to the unburnt mixture reads, for example (Clavin &Williams, 1982and Matalon & Matkowsky, 1982)
Here
is the Zeldovich number, where E is the ac7va7on energy, and Le is the
Lewis number of the decient reactant
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The Lewis number is approximately unity for methane ames and largerthan unity for fuel-rich hydrogen and all fuel-lean hydrocarbon ames
other than methane
Therefore, since the rst term on the r.h.s. of
is always posi7ve, the Markstein length is posi7ve for most prac7cal
applica7ons of premixed hydrocarbon combus7on, occurring typically
under stoichiometric or fuel-lean condi7ons
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Whenever the Markstein length is nega7ve , as in lean hydrogen-air mixtures,diffusional-thermal instabili7es tend to increase the ame surface area
This is believed to be an important factor in gas cloud explosions of hydrogen-
air mixtures
Although turbulence tends to dominate such local effects the combus7on ofdiffusional-thermal instabili7es and instabili7es induced by gas expansion
could lead to strong ame accelera7ons
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Strain Effect on Laminar Burning Velocityfrom Numerical Simula7ons
Laminar premixed stoichiometricmethane/air counterow ames
Curvature Effect on Laminar BurningVelocity from Experiments and Theory
Effects of curvature and strain on laminar burning velocity
Laminar premixed stoichiometricmethane/air spherically expanding
ames
Note: sL,u sL,b/
= 0.8
= 1
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Introducing
into the G-equa7on, it may be wri en as
Here
is dened as the Markstein diffusivity
The curvature term adds a second order deriva7ve to the G-equa7on
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This avoids the forma7on of cusps that would result from
for a constant value of sL0
While the solu7on of the G-equa7on with a constant sL0 is solely determinedby specifying the ini7al condi7ons, the parabolic character of
requires that the boundary condi7ons for each iso-surface G must be
specied
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The G-equa7on model in the corrugated amelets regime Flame thin compared to small turbulent scales Level set describes interface between unburned and burned Flame structure embedded in the interface, but varia7ons on much
smaller scale Mul7-scale model
G-eld dened as distance func7on
Buschmann 1996
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The Level Set Approach for the Thin Reac=on Zones Regime
The equa7on
is suitable for thin ame structures in the corrugated amelets regime, En7re ame structure quasi-steady Laminar burning velocity well dened
However, not suitable for thin reac7on zones regime
Deriva7on of level set equa7on valid in the thin reac7on zones
regime
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Since the inner layer shown previously is responsible for maintaining the
reac7on process alive, we dene the thin reac7on zone as the inner layer
The loca7on of the inner layerwill be determined by the
iso-scalar surface
of the temperature se ng
T ( x ,t )=T 0, where T 0 is the
inner layer temperature
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The temperature equa7on reads
where D is the thermal diffusivity T the chemical source term
Similar to
for the scalar G, the iso-temperature surface T ( x ,t )=T 0 sa7ses the condi7on
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Gibson (1968) has derived an expression for the displacement speed sd of aniso-surface of non-reac7ng diffusive scalars
Extending this result to the reac7ve scalar T this leads to
where the displacement speed sd is given by
Here the index 0 denes condi7ons immediately ahead of the thin reac7onzone
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The normal vector on the iso-temperature surface is dened as
We now want to formulate a G-equa7on describing the loca7on of the thinreac7on zones such that the iso-surface T( x ,t )=T0 coincides with the iso-
surface dened by G( x ,t )=G0
Then, the normal vector dened by
is equal to that dened by
and also points towards the unburnt mixture
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Using and
together with
leads the G-equa7on
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Peters et al. (1998) show that the diffusive term appearing in the brackets in
this equa7on may be split into one term accoun7ng for curvature and anotherfor diffusion normal to the iso-surface
This is consistent with the deni7on of the curvature
if the iso-surface G( x ,t )=G0 is replaced by the iso-surface T ( x ,t )=T 0 and
if D is assumed constant
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Introducing
into
one obtains
Here
is to be expressed by in terms of the G-eld
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The quan77es sn and sr are contribu7ons due to normal diffusion and reac7onto the displacement speed of the thin reac7on zone and are dened as
In a steady unstretched planar laminar ame we would have
In the thin reac7on zones regime, however, the unsteady mixing and diffusion
of chemical species and the temperature in the regions ahead of the thinreac7on zone will inuence the local displacement speed
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Then the sum of
is a uctua7ng quan7ty that couples the G-equa7on to the solu7on of the
balance equa7ons of the reac7ve scalars
There is reason to expect, however, that sL,s is of the same order of magnitudeas the laminar burning velocity
The evalua7on of DNS-data by Peters et al. (1998) conrms this es7mate
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In that paper it was also found that the mean values of sn and sr slightlydepend on curvature
This leads to a modica7on of the diffusion coefficient which partly takesMarkstein effects into account
We will ignore these modica7ons here and consider the following level setequa7on for ame structures of nite thickness
This equa7on is dened at the thin reac7on zonev , sL,s, and D are values at that posi7on
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The G-equa7on in the thin reac7on zones regime
is very similar to that for the corrugated amelets regime
Important is the difference between and D and the disappearance of thestrain term
The la er is implicitly contained in the burning velocity sL,s
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In an analy7cal study of the response of one-dimensional constant densityames to 7me-dependent strain and curvature, Joulin (1994) has shown that
in the limit of high frequency perturba7ons, the effect of strain disappears
en7rely and Lewis-number effects also disappear in the curvature term such
that
This analysis was based on one-step large ac7va7on energy asympto7cs withthe assump7on of a single thin reac7on zone
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The important difference between the level set formula7on
and the equa7on for the reac7ve scalar
is the appearance of a burning velocity which replaces normal diffusion and
reac7on at the ame surface
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It should be noted again that the level set equa7ons
and
are only dened at the ame surface,while
is valid in the en7re eld
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The G-equa7on model in the thin reac7on zones regime Flame broadened by turbulence, but Reac7on zone s7ll thin compared to turbulent scales and appears as
interface Level set describes loca7on of reac7on zone
DNS of Premixed Combus7on, Knudsen 2010
Level set describing thinreac7on zone
Burned gasBroadened preheat zone
Unburned gas
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A Common Level Set Equa=on for Both Regimes
The G-equa7on applies to different regimes in premixed turbulentcombus7on:
Corrugated amelets regime
Thin reac7on zones regime
In order to show this, we will analyze the order of magnitude of the differentterms in the second equa7on
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This can be done by normalizing the independent variables and the curvaturein this equa7on with respect to Kolmogorov length, 7me and velocity scales
Using 2/ t = one obtains
In ames, D/ is of order unity
Since Kolmogorov eddies can perturb the ow as well as the G-eld, allderiva7ves, the curvature and the velocity v * are typically of order unity
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However, since sL,s is of the same order of magnitude as sL, the deni7on
shows that the ra7o sL,s/ v is propor7onal to Ka -1/2 .
Since Ka > 1 in the thin reac7on zones regime, it follows for this regime that
In the thin reac7on zones regime , the propaga7on term in the equa7on
is therefore small and the curvature term will be dominant
In the corrugated amelets regime , sL,s/ v becomes large and propaga7ondominates
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We want to base the following analysis on an equa7on which contains onlythe leading order terms in both regimes
Therefore we take the propaga7on term with a constant laminar burningvelocity sL0 from the corrugated amelets regime and the curvature term
mul7plied with the diffusivity D from the thin reac7on zones regime
The strain term will be neglected in both regimes
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The leading order equa7on valid in both regimes then reads
For consistency with other eld equa7ons that will be used as a star7ng pointfor turbulence modeling, we have mul7plied all terms in this equa7on with .
This will allow to apply Favre averaging to all equa7ons
Furthermore, we have set sL0 = u sL,u constant and denoted this byparanthesis
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Modeling Premixed Turbulent Combus=on Based on the Level Set Approach
If the G-equa7on is to be used as a basis for turbulence modeling, it isconvenient to ignore at rst its non-uniqueness outside the surface G( x , t ) =
G0.
Then the G-equa7on would have similar proper7es as other eld equa7onsused in uid dynamics and scalar mixing
This would allow to dene, at point x and 7me t in the ow eld, a probabilitydensity func7on P(G; x ,t ) for the scalar G
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Then, the probability density of nding the ame surface G( x ,t )=G0 at x and t is given by
This quan7ty can be measured, for instance, by coun7ng the number of amecrossings in a small volume V located at x over a small 7me difference t
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Experimental data for the pdf (Wirth et al., 1992, 1993) from a transparentspark-igni7on engine
Smoke par7cles, which burntout immediately in the ame
front, were added to the
unburnt mixture
Thereby, the front could bevisualized by a laser sheet as
the borderline of the region
where Mie sca ering of
par7cles could be detected The pdf represents the pdf of
uctua7ons around the mean ame contour of several instantaneous images
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By comparing the measured pdf with a Gaussiandistribu7on, it is seen to be slightly skewed to the
unburnt gas side
This is due to the non-symmetric inuence of thelaminar burning velocity on the shape of the ame
front
There are rounded leading edges towards
the unburnt mixture, but sharp and narrow
troughs towards the burnt gas
This non-symmetry is also found in otherexperimental pdfs
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Without loss of generality, we now want to consider a one-dimensionalsteady turbulent ame propaga7ng in x -direc7on
We will analyze its structure by introducing the ame-normal coordinate x ,such that all turbulent quan77es are a func7on of this coordinate only
Then, the pdf of nding the ame surface at a par7cular loca7on x within the
ame brush simplies to P(G0; x ), which we write as P( x )
We normalize P( x ) by
and dene the mean ame posi7on x f as
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The turbulent ame brush thickness can also be dened using P( x )
With the deni7on of the variance
a plausible deni7on is
We note that from P( x ) two important proper7es of a premixed turbulentame, namely the mean ame posi7on and the ame brush thickness can be
calculated
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Peters (1992) considered turbulent modeling of the G-equa7on in thecorrugated amelets regime and derived Reynolds-averaged equa7ons for the
mean and the variance of G
The main sink term in the variance equa7on was dened as
This quan7ty was called kinema7c restora7on in order to emphasize theeffect of local laminar ame propaga7on in restoring the G-eld and thereby
the ame surface
Corruga7ons produced by turbulence, which would exponen7ally increase theame surface area with 7me of a non-diffusive iso-scalar surface are restored
by this kinema7c effect
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From that analysis resulted a closure assump7on which relates the main sinkterm to the variance of G and the integral 7me scale
where c =1.62 is a constant of order unity
This expression shows that kinema7c restora7on plays a similar role inreducing uctua7ons of the ame front as scalar dissipa7on does in reducing
uctua7ons of diffusive scalars
It was also shown by Peters (1992) that kinema7c restora7on is ac7veat the Gibson scale, since the cut-off of the iner7al range in the scalar
spectrum func7on occurs at that scale
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Equa=ons for the Mean and the Variance of G
In order to obtain a formula7on that is consistent with the well-establisheduse of Favre averages in turbulent combus7on, we split G and the velocity
vector v into Favre means and uctua7ons
Here, the Favre means are at rst viewed as uncondi7onal averages
At the end, however, only the respec7ve condi7onal averages are of interest
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The turbulent burning velocity sT 0 is obtained by averaging over
By se ng one nds for the sta7onary unstretched ame front
Using a number of addi7onal closure assump7ons described in Peters (2000),one nally obtains the following equa7ons for the Favre mean and variance of
G:
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It is easily seen that
has the same form as
and therefore shares its mathema7cal proper7es
It also is valid at only
The solu7on outside of that surface depends on the ansatz for the Favre meanof G that is introduced
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In order to solve
a model for the turbulent burning velocity s0T must be provided.
A rst step would be to use empirical correla7ons from the literature
Alterna7vely, a modeled balance equa7on for the mean gradient will bederived next
According to Kerstein (1988), this quan7ty represents the ame surface areara7o , which is propor7onal to the turbulent burning velocity
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