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Flame-vortex interaction: Effect of residence time and

formulation of a new efficiency function

F. Thiesset, G. Maurice, F. Halter, N. Mazellier, C. Chauveau, I. Gökalp

To cite this version:

F. Thiesset, G. Maurice, F. Halter, N. Mazellier, C. Chauveau, et al.. Flame-vortex interaction:

Effect of residence time and formulation of a new efficiency function. Proceedings of the Combustion

Institute, Elsevier, 2017, 36 (2), pp.1843 - 1851. �10.1016/j.proci.2016.06.172�. �hal-01660275�

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Flame-vortex interaction : e

ffect of residence time and formulation of a

new e

fficiency function

F. Thiesseta, G. Mauricea,b, F. Halter∗a, N. Mazellierb, C. Chauveaua, I. G¨okalpa aCNRS ICARE, Avenue de la Recherche Scientifique, 45072 Orl´eans Cedex 2 France bUniversity of Orl´eans, INSA de Bourges, PRISME, EA 4229, 45072 Orl´eans, France

Abstract

In this study, a combined experimental and numerical investigation of a toroidal vortex interacting with a stag-nation premixed flame is carried out with the aim of quantifying the ability of such a vortex to stretch the flame. By scrutinizing the literature, it was found that, although inferred from exactly similar numerical simulations, existing parametric expressions for the efficiency function (the ratio of the flame stretch to vortex strain) do not agree in the way the latter should behave when the ratio of the vortex rotational velocity Uθto the laminar flame speed SL

is increased. These expressions also appear to be unequally accurate when compared to experimental data and do not feature the non monotonic evolution of the efficiency function with Uθ/SLwhich is observed in both

experi-mental data and numerical simulations of a ’isothermal’ propagating interface. In addition, whilst previous studies have focused only on the impact of Uθ/SLand Rv/δL(Rvbeing the vortex typical size and δLthe laminar flame

thickness) our study reveals the importance of other parameters, the most important of which being the residence time of the vortex associated with its convection velocity. These results yield a new formulation for the efficiency function which compares favourably well with experimental data.

Keywords: Flame vortex interactions, Flame stretch, Vortex strain, residence time

Corresponding author at: CNRS ICARE, Avenue de la Recherche Scientifique, 45072 Orl´eans Cedex 2 France Email: fabien.halter@cnrs-orleans.fr (F. Halter)

∗∗Colloquium : TURBULENT FLAMES

Total length= 6126 words (Method 2) Main text= 4231 words

Nomenclature= 0 word References= 253 words Figure 1 to 10= 198, 207, 132, 161, 136, 147, 191, 125, 191, 154 words Tables= 0 word No color reproduction

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1. Introduction

1

Understanding and predicting the different

mech-2

anisms at play in turbulent premixed flames is a

3

tremendously difficult challenge. The main reason

4

is that there is still a lack of knowledge of the

tur-5

bulent flow structure which features a large variety

6

of turbulent scales. A given eddy thus experiences

7

many different processes induced by turbulent scales

8

of different sizes, such as vortex stretching and

sweep-9

ing, diffusion by viscosity, these effects being

partic-10

ularly arduous to model. In addition, when reacting

11

flows are concerned, the flame does not act as a

pas-12

sive scalar because of its propagative character and

13

the inherent heat release that locally modifies the fluid

14

physical properties. The high local flame curvature

15

and strain, also impact its local consumption or

dis-16

placement speed in a way which remains poorly

un-17

derstood.

18

There is thus a need for fundamental investigations

19

of the interactions between the fluid motion and a

20

flame in simplified and well controlled situations. One

21

of these is the case of a flame interacting with a single

22

vortex dipole (see the review by Renard et al. [1]).

Pi-23

oneer studies of Flame-Vortex Interactions (hereafter

24

abbreviated by FVI) emerged in the 90’s with notably

25

Poinsot et al. [2], Roberts and Driscoll [3], Wu and

26

Driscoll [4], Roberts et al. [5], Lee and Santavicca [6]

27

and more recently with Renard et al. [1], Colin et al.

28

[7], Charlette et al. [8], Bougrine et al. [9].

29

Although some effects such as vortex stretching,

30

sweeping, tilting are not present, FVI are expected to

31

mimic, at least partly, the processes at play in real

tur-32

bulent flames. The aforementioned investigations on

33

FVI have led notably to the construction of the

so-34

called spectral diagrams which allows to identify the

35

conditions needed for a vortex to stretch the flame, to

36

create pockets of fresh gas or to locally quench the

37

flame. In addition, these results yielded expression of

38

efficiency functions, i.e. the transfer function between

39

vortex strain and flame stretch. In this prospect, Colin

40

et al. [7], Charlette et al. [8] have focused on the

ef-41

fect of vortex size Rvrelative to the flame thickness δL

42

and vortex rotational velocity Uθrelative to the flame

43

speed SL. More recently, the effect of Lewis number

44

has been incorporated by Bougrine et al. [9]. These

45

efficiency functions are extremely valuable as they are

46

widely used in LES of turbulent premixed combustion

47

in order to model the sub-grid scale wrinkling factor

48

[7–9].

49

The aim of the present study is to explore one

par-50

ticular aspect of the interaction between the flow

mo-51

tion and a flame, which we referred to as the

strain-52

sweeping competition(see for instance the review by

53

Driscoll [10]). This competition can be

conceptu-54

ally described in terms of time-scales. Based on

phe-55

nomenological arguments [11], the strain-based time

56

scale τs of a scale r with characteristic velocity ur is

57

τs ∝ r/ur ∝ r2/3. This time-scale is generally

re-58

ferred to as the eddy turn-over time. Previous studies

59

devoted to FVI investigations [2–9] indicate that the

60

smaller this time scale, the larger is the flame stretch.

61

On the other hand, Tennekes [12] suggested that

an-62

other relevant time scale in a turbulent flow relates to

63

the sweeping effect by energy-containing eddies. He

64

pointed out that a given scale of size r is convected

65

by the large scales, i.e. with characteristic velocity

66

of the order of u0, the root-mean-square of the

veloc-67

ity fluctuations. The sweeping time scale as called by

68

Tennekes [12] thus writes τc ∝ r/u0. This has been

69

verified experimentally by e.g. Poulain et al. [13]. It

70

is worth stressing that these two phenomenology both

71

lead to the same prediction for the scaling exponent

72

of the energy spectra and are therefore

undistinguish-73

able in spectral space. In the field of combustion the

74

sweeping time scale is somehow related to the

resi-75

dence time [10] and basically describes the duration

76

of the interaction of a vortex located in the vicinity

77

of the flame. As far as the sweeping (or residence)

78

time scale is concerned, FVI [3, 4] corroborates the

79

intuitive statement that the smaller this time scale, the

80

smaller the flame stretch since the vortex spends less

81

time in the vicinity of the flame for rolling it up. In

tur-82

bulent flames, there is thus a competition between

tur-83

bulent strain and turbulent convection, the latter

phe-84

nomenon acts in decreasing the flame stretch whereas

85

the former has the opposite effect. It is thus worth

86

investigating these effects independently in order to

87

give further insight into their respective influence on

88

the flame. Further, a more complete expression for

89

the efficiency function which accounts for both strain

90

and residence time effects could be derived and used

91

in LES.

92

In the present study, a new experimental set-up was

93

designed in the goal of quantifying the degree of the

94

interactions between a vortex dipole and a stagnation

95

premixed flame. Some simple numerical simulations

96

based on the ’isothermal’ G-equation, have been

fur-97

ther carried out and validated against experimental

98

data. Such simulations allow to assess the effect of

99

the convection velocity and rotational velocity

inde-100

pendently. Finally, the respective effect of these two

101

phenomena on flame stretch are separately quantified,

102

incorporated into a new formulation for the efficiency

103

function, and compared to experimental data.

104

2. Experimental apparatus

105

Investigations are carried out in a single jet

stagna-106

tion flame configuration which is a modified version

107

of that used by Bouvet et al. [14]. A schematic of the

108

burner is provided in Fig. 1. A laminar strained flame

109

is stabilized against a 4-mm-thick stainless steel plate.

110

The stagnation plate is attached to an alumina foam

111

plug selected for its insulating properties. The fuel

112

and oxidizer are introduced through the side of the

113

burner. A so-called ’particle diffuser cone’ filled with

114

6 mm glass beads is used to ensure a homogeneous

115

mixture in the nozzle plenum. The reactive mixture

116

then flows into the burner plenum through a 5 mm

117

thick aluminium grid. It is finally accelerated in the

118

(4)

Figure 1: Schematic of the experimental setup

converging section with a D= 15mm outflow

diame-119

ter, creating an upward-oriented jet with a nearly top

120

hat velocity profile at the burner exit. The

burner-to-121

stagnation plate distance L was fixed to 25mm, given a

122

L/D ratio greater than unity as usually recommended.

123

Moreover, it allows to stabilize flames sufficiently far

124

from the plate to track the flame/vortex interaction

125

without being affected by the plate. To avoid external

126

perturbations and improve flame stability, a laminar

127

coaxial shroud of nitrogen is used. The nitrogen flow

128

rate was set so that the coflow exit velocity closely

129

matches that of the main flow. In the present study,

130

the wall stagnation configuration is preferred over the

131

classical opposed jet configuration for the following

132

reasons: (i) the experimental apparatus can be

im-133

plemented and controlled easily (no need for upper

134

burner) and (ii) wall-stabilized flames are generally

135

found to be more stable than counterflow ones.

136

The toroidal vortex is generated by applying a

sud-137

den pressure discharge of reactive mixture of same

138

equivalence ratio than the main flow in a tube of 2mm

139

in diameter located on the centerline of the flow and

140

35mm upstream the burner outlet (Fig. 1). The

in-141

tensity of the vortex is controlled by varying the

pres-142

sure magnitude within a pressurized tank located

up-143

stream. To control the duration of the pressure

dis-144

charge, it was necessary to use two electro-valves

145

placed one after another because the time needed for

146

a single electro-valve to open and close was too large.

147

First, the upstream electro-valve is kept closed while

148

the second placed downstream is opened. Then, for

149

generating the vortex, the first valve is opened while

150

the second one is closed with a small time delay, so

151

that the pressure discharge duration was about 5ms.

152

Three equivalence ratios for the reactive

methane-153

air mixture φ= 1, 0.9, 0.8 have been considered. The

154

Figure 2: Time sequence of Mie scattering images of a typ-ical FVI (Uθ/SL = 1.43). The flame contours and

vortic-ity field are superimposed. The top of each image has been cropped to show only the first 20mm. The line corresponds to the flame contours with area A(t,∆) estimated over a domain of width∆. Uθ, Ucare the vortex rotational and convection

respectively, whilst Rvis the vortex core-to-core distance.

laminar flame speed and thickness have been

eval-155

uated using the GRI-mech 3.0 mechanism together

156

with the stagnation flame module of the CHEMKIN

157

Pro software. The temperature of the wall, measured

158

by Bouvet et al. [14], was set to 800K. It was found

159

that SL = 40.3, 36.5, 30.6cm.s−1and δL = 433, 463,

160

525µm respectively for φ= 1, 0.9 and 0.8. The strain

161

rate was respectively 90, 86 and 77s−1for φ= 1, 0.9

162

and 0.8.

163

The flame front is tracked by means of Mie

scat-164

tering laser tomography. Seeding of the flow is made

165

by silicon oil droplets supplied by an atomizer.

Typ-166

ical size of droplets is about 1µm. It was checked

167

that the flame location was the same when the seeding

168

was turned off suggesting that the laminar flame speed

169

was not altered by the addition of silicon droplets in

170

the flow. Then, use is made of a continuous Coherent

171

Verdi G20 Laser which delivers up to 20W at 532nm.

172

The light scattered by the droplets is then captured by

173

a Phantom V1210 camera, equipped with a 105mm

174

F2.8 lens, working at an acquisition rate of 23005Hz

175

with a field of view of 704×640 pixels2and the

reso-176

lution was 38µm/px.

177

The flame contour is then extracted as follows.

178

Firstly, a contrast-limited adaptive histogram

equal-179

ization (CLAHE) is applied to the original images in

180

order to optimize the contrast in the images. Then, to

181

limit the pixelization associated with the CLAHE,

im-182

ages are filtered using a Gaussian filter of size equal

183

to 4 times the spatial resolution. For the binarizing

184

procedure, we use a standard threshold-based

tech-185

nique. More precisely, the histogram of the gray scale

186

is calculated. The latter reveals two distinct peaks

cor-187

responding to the fresh and burned gas respectively.

188

The threshold value for discriminating the flame

(5)

tour is set as the average value between the gray scale

190

of these two peaks. This yields estimations for the

191

progress variable, noted c, which is by definition 0 and

192

1 in the unburned and burned gas respectively. The

ve-193

locity field within the unburned mixture is estimated

194

by classical 2D-2C Particle Image Velocimetry (PIV).

195

For this purpose, the Matlab subroutines of Thielicke

196

and Stamhuis [15] were used. A time sequence of Mie

197

scattering images at four distinct instants is shown in

198

Fig. 2. The vorticity field and flame contours are

su-199

perimposed. The time t0= 0 was set arbitrarily as the

200

time t where the vortex center was 2.5mm downstream

201

the burner outlet. One observes that at a time t=4ms,

202

the flame is rather flat suggesting that the vortex

gen-203

erator is sufficiently far from the burner outlet for not

204

creating a wake. As the vortex is convected (t=6ms

205

and 8ms), the flame is increasingly stretched. Its area

206

then reaches a maximum before decreasing (t=10ms)

207

while the flame goes back to its original position.

208

The vortex parameters, i.e. the circumferential

ve-209

locity Uθ, the convection velocity Uc and the

core-210

to-core distance Rv, have been inferred from PIV by

211

fitting the velocity field calculated with an Oseen

vor-212

tex. Our experimental set-up allows to cover the

213

range 0.5 . Uθ/SL . 2.5 whereas Rv/δL slightly

214

varies around 6.5. Our database thus lies between

215

the no-effect limit and the quenching limit assessed

216

by Roberts et al. [5].

217

3. Experimental results

218

3.1. Domain size effects

219

The focus of this paper is on the flame stretch

as-220

sociated with the interaction with a vortex. Given the

221

vortex rotational velocity Uθand the distance between

222

vortex cores Rv(see Fig. 2), the vortex strain is

gener-223

ally estimated as Uθ/Rv[7–9]. On the other hand, the

224

flame stretch is evaluated as

225

K(t,∆) = 1 A(t,∆)

∂A(t, ∆)

∂t (1) where, thanks to axisymmetry, A(t,∆) =

226

R

y(s)px02+ y02ds is the flame area at a time t

227

evaluated over a domain of width ∆ (see Fig. 2).

228

s is the curvilinear parameter, y and x are the

229

flame contour spatial coordinates and the prime

230

denotes derivatives with respect to s. Then the

231

efficiency function is defined as in [7–9], viz.

232

C(∆) = Kmax(∆)/ (Uθ/Rv), where Kmax(∆) is the

233

maximum value of K(t,∆). The appearance of

234

∆ in the efficiency function is new. In previous

235

numerical studies [7–9] a given value for∆ ≈ 6Rv

236

corresponding to the size of the simulation domain

237

was chosen. However, it appears straightforward

238

that Kmaxdepends on∆. Indeed, because the portion

239

of flame interacting with the vortex is constant (i.e.

240

there exists a∆ above which ∂A/∂t is independent of

241

∆), we expect Kmax to decrease with∆2since A(t,∆)

242

monotonically increases with∆2. Figure 3 presents

243 1 2 3 4 5 6 0 0.5 1 1.5 2 ∆/Rv C = Km a x / (U θ / Rv ) Fit Eq. ( 2) Expe r ime nt s

Figure 3: Evolution of Kmaxwith∆ for Uθ/SL= 1.43.

Sym-bols represent experimental data whilst the line corresponds to the fit using Eq. (2).

the evolution of Kmax with respect to∆. It clearly

244

appears that Kmax rapidly decreases with respect to

245

∆ and for ∆ sufficiently large (i.e. for ∆ larger to a

246

certain∆i), it is found that Kmaxfollows the relation

247 Kmax= Kmax0 " i−∆0 ∆ − ∆0 #2 . (2)

In Eq. (2), ∆i represents the domain width above

248

which ∂A/∂t is constant and∆0is interpreted as a

vir-249

tual origin, i.e. K−1

max → 0 when∆ → ∆0. From our

250

experimental database, it was found that ∆i/Rv and

251

∆0/Rvwere constant and are equal to 2.5 ± 0.05 and

252

−0.5 ± 0.1 respectively.

253

Figure 3 emphasizes that the values for the

effi-254

ciency function that were previously provided notably

255

by Colin et al. [7], Charlette et al. [8], Bougrine et al.

256

[9], were inferred for a given value of∆/Rvwhereas

257

they should depend on∆. In other words, if they had

258

chosen a different value for the simulation domain,

259

they would have obtained different values. Moreover,

260

the no-effect limit assessed by Poinsot et al. [2] which

261

”corresponds to vortices which induce a maximum

262

modification of the total reaction rate of about 5

per-263

cent”, should also depend on∆.

264

3.2. Impact of vortex intensity

265

We now turn our attention to the effect of the

vor-266

tex strength on the flame stretch. Figure 4 depicts the

267

evolution of C0 = K0

max/(Uθ/Rv) as a function Uθ/SL

268

(hereafter the superscript0 on C will be removed for

269

the sake of simplicity). Experimental results are also

270

compared to the predictions provided by Colin et al.

271

[7], Charlette et al. [8], Bougrine et al. [9] which are

272

respectively noted Cco, Cch and Cb. Their respective

273

analytical expressions are not recalled here but the

274

reader can refer to [7–9] for more details.

275

Experimental uncertainties have been estimated as

276

follows. The precision of the subpixel interpolation of

277

the PIV algorithm is generally about 0.05 pixel. The

278

uncertainty on the velocity field is therefore constant

279

and equals to about 0.04m.s−1provided the resolution

280

and sampling frequency of our images. The error on

281

the estimation of Rvprovided by fitting experimental

282

(6)

0.5 1 1.5 2 2.5 0.75 1 Uθ/SL C = K 0 ma x / (U θ / Rv ) Cc h Cb Cc o

Figure 4: Efficiency function C = K0

max/(Uθ/Rv) as a

func-tion of Uθ/SL. The lines labbeled Cco, Cch, Cb correspond

respectively to the parametric expressions provided by Colin et al. [7], Charlette et al. [8], Bougrine et al. [9], corrected us-ing Eq. (2) to obtain K0

max. The circle symbols correspond to

the present measurements whilst the square symbol is taken from Bougrine et al. [9]

data with an Oseen vortex was generally of about 4%.

283

The uncertainty in the determination of Kmaxwas

sup-284

posed to be negligible by comparison with the errors

285

on both Uθand Rvsince A is readily measurable.

286

A careful analysis of Fig. 4 first reveals that,

al-287

though rather limited, some departures between

ex-288

perimental data and the predictions of either [7–9]

289

can be observed. By comparison with experiments,

290

the efficiency function of Colin et al. [7] appears to

291

be the more appropriate. These differences might be

292

explained by several parameters. First, it is worth

293

recalling that our configuration is axisymetric whilst

294

DNS of [7–9] are 2D (planar). Secondly, in [7–9],

295

the flame stretch is estimated from the heat release

296

Q, i.e. K = Q−1dQ/dt which implicitly suggests

297

that Refs. [7–9] considered that the flame

consump-298

tion speed was unaltered by the flame stretch. Such

299

an hypothesis is consistent with LES models based

300

on the flame density concept for which the heat

re-301

lease or fuel consumption is calculated through the

302

laminar flame speed multiplied by the flame surface

303

density. This assumption is however not consistent

304

with LES that employs skeletal or analytical

chem-305

istry which explicitly accounts for the effect of stretch

306

on the flame consumption speed.

307

Fig. 4 also suggests that though based on exactly

308

similar simulations, existing parametric expressions

309

do not agree in the way C should behave with

re-310

spect to Uθ/SL. Indeed, Colin et al. [7], Charlette

311

et al. [8] both predict an increasing tendency of C

312

with respect to Uθ/SL whereas Cb leads to the

op-313

posite trend. Although slightly scattered, our

exper-314

imental data further suggest that the evolution of C is

315

non monotonic, i.e. C first increases before decreasing

316

slightly for Uθ/SLlarger than about 1.5. The

decreas-317

ing tendency of C was also observed in the DNS of

318

Bougrine et al. [9] when the vortex strength was

en-319

hanced from Uθ/SL= 0.8 to 8 (note that there is a nice

320

agreement between our experiments and the DNS data

321

of Bougrine et al. [9] for Uθ/SL = 0.8, Rv/δL = 5).

322

This observation can be readily explained by recalling

323 0 0.5 1 1.5 2 2.5 3 0 0.5 1 1.5 Uθ/SL { Uc − U u(X c )} / SL (Uθ/SL)2 / 3

Figure 5: Convection velocity Uc− Uu(Xc), where Uu(Xc) is

the streamwise velocity of the unperturbed flow at the vortex center location Xc, as a function of Uθ. The dotted line is given by 0.5(Uθ/SL)2/3.

that an intense vortex will create high local curvatures

324

which act in decreasing the total stretch of the flame.

325

In other words, increasing the vortex strength can be

326

less efficient since it leads to too high curvatures that

327

globally reduces the flame stretch.

328

Roberts and Driscoll [3] were first to realize that

329

the flame stretch is also driven by the convection

ve-330

locity Ucof the vortex dipole. More precisely, they

331

suggested that for a given Uθ, increasing Uc yields

332

a smaller flame stretch because the residence time of

333

the vortex in the vicinity of the flame decreases. This

334

intuitive statement was further confirmed by Wu and

335

Driscoll [4] on the basis of numerical simulations of

336

a propagating surface. There is thus a need for

incor-337

porating these two opposed effects (convection vs

ro-338

tational velocity) into a more complete expression of

339

the efficiency functions. However, in our experiments,

340

it was observed that increasing Uθirremediably led to

341

a higher convection velocity consistently with

analyt-342

ical studies (see [1] and references therein). It was

343

found experimentally (Fig. 5) that the convection

ve-344

locity Uc− Uu(Xc) (Uu the streamwize velocity

ex-345

perienced by the vortex located at Xc) scales as Uθ2/3.

346

Therefore, it is not possible from experiments to

as-347

sess independently the respective influence of Uθand

348

Uc.

349

Consequently, following e.g. Wu and Driscoll [4]

350

or Lee and Santavicca [6], we decided to perform

sim-351

plified numerical simulations of the same burner in

352

the goal of studying the effect of Ucand Uθ

indepen-353

dently. These simulations have been widely used in

354

the past mainly because they are extremely low-cost

355

in terms of computational resources. Indeed, they

356

consider the flame as a ’passive’ propagating

(ther-357

mally neutral) interface, which tremendously reduces

358

the problem complexity. Such simulations neglect the

359

heat release and therefore many physical mechanisms

360

are not taken into account. First, the higher viscosity

361

due to high temperature in the burnt gas, resulting in

362

a larger dissipation rate is not accounted for.

Baro-363

clinic effects as evidenced by [5] are also neglected.

364

However, with this limitations in mind, one aspect of

365

the present work is to investigate in detail how

(7)

0 0.002 0.004 0.006 0 0.5 1 1.5 2 t[s ] Rv 2[mm] Uc[m/s ] Xc[c m] Uθ[m/s ] Uc−Uu( Xc) [m/s ]

Figure 6: Time evolution of the vortex parameters for a given case in the database. The vortex core-to-core distance Rv, the

convection velocity Ucand Uc− Uu(Xc), the vortex center

streamwize position Xc, and the rotational velocity (black)

are represented as a function of time. Symbols are experi-mental data whilst lines stand for the simulation.

istic these (widely used) simulations could be when

367

compared to experiments. In other words, handling

368

such a comparison helps in giving further insights into

369

the importance of heat release and associated physical

370

mechanism during a FVI.

371

4. Simulations of a vortex interacting with a

372

propagating interface

373

4.1. Implementation and validation

374

Present numerical simulations consider the flame

375

as a two-dimensional (axisymmetric) propagating

in-376

terface convected by the fluid motion U while

advanc-377

ing at the laminar flame speed SL. The kinematic

re-378

lationship between the flame and the flow field is then

379

given by the G-equation which writes [4, 6]

380

∂G

∂t +U.∇G = SL|∇G|. (3)

In the present case, the Navier-Stokes are not

ex-381

plicitly resolved and the velocity field is set as

fol-382

lows. First, Uu and Vu, i.e. the velocity component

383

in the streamwise x and transverse y direction of

un-384

perturbed flow (before the generation of the vortex)

385

is given by Uu(x, y) = −2 R a(x)dx and Vu(x, y) =

386

a(x) × y, where U0 = 1.23m.s−1is the inlet velocity

387

of the burner and a(x)= ∂Vu/∂y(y = 0) is the

trans-388

verse strain of the unperturbed flow. a(x) was fitted

389

from experiments using a second order polynomial.

390

The coefficients of the polynomial were adjusted for

391

each equivalence ratio.

392

Secondly, the vortex velocity field was added to Uu

393

and Vuand set using the Oseen expression. The

in-394

put parameters for the Oseen vortex are Uθ, Xc (the

395

streamwize location of the vortex center) and Rv, the

396

core-to-core distance. In the present case, by

analyz-397

ing experimental data (see Fig. 6), it was found that

398

Uθ does not vary with time and was therefore set to

399

a constant. The vortex center Xcwas convected at a

400

velocity Uc, viz. ∂Xc/∂t = Uc, where Uc− Uu(Xc)

401 0.002 0.004 0.006 0.008 0.01 0.012 −100 −50 0 50 100 time t [s ] K (t ) # s − 1 $ 0 10 20 30 40 A (t ) − A (t0 ) [m m 2] G e quat ion Expe r ime nt s Uθ/SL= 1.43 Uθ/SL= 1.83 Uθ/SL= 0.94 Uθ/SL= 0.94 Uθ/SL= 1.43 Uθ/SL= 1.83

Figure 7: Time evolution of the flame area A(t,∆) (a) and stretch K(t,∆) (b) for ∆ = 10mm, for three different ratio of Uθ/SL= 0.94, 1.43, 1.83. Dashed and full lines correspond

respectively to experimental and numerical data

0 100 200 300 400 0 100 200 300 400 K0 m a x#s− 1$ measur ed K 0 ma x # s − 1 $ G e q u a ti o n 0 1 2 3Uθ SL

Figure 8: Maximum stretch K0

max assessed by experiments

versus K0maxinferred from numerical simulations. Symbols

are coloured by Uθ/SL

was found to be constant (see Fig. 6). The time

evolu-402

tion of the vortex ring diameter Rvfollows the relation

403

[16] R−1

v ∂Rv/∂t = a(Xc). In Fig. 6, the time

evolu-404

tion of vortex parameters issued from the experiments

405

are compared to that prescribed in the numerical

sim-406

ulations. All quantities compare extremely well and

407

thus validate the procedure for establishing the

veloc-408

ity field.

409

The G-field was initialized as a signed distance

410

with the iso-value G = G0 = 0 located at the

411

streamwize location x at which Uu(x)= S

L.

Equa-412

tion (3) is resolved using a fifth-order WENO

dis-413

cretization scheme in space and 4th-order

Runge-414

Kutta scheme for time advancement. The usual

reini-415

tialization procedure is also applied at each time step

416

so that the G-field remains a signed distance. The

417

mesh size is 500×500 corresponding to a domain

418

size of 25×25mm2. It was checked that increasing

419

the mesh size up to 1000×1000 points yielded only

420

marginal differences.

421

Numerical simulations have been validated against

422

experimental data. Results for three different values

423

(8)

0 1 2 3 4 5 0.2 0.4 0.6 0.8 1 Uθ/SL C = K 0 ma x / (U θ / Rv ) 0 2 4 6 8 10 12 0 0.5 1 U= (Uθ/SL) × (Uc∗/Uθ)4 / 3 F = C × (U ∗/c SL ) 1 / 3 (b) (a) Cc h Cc o Cb Uc/SL

Figure 9: (a) Efficiency function as a function of Uθ/SLfor

different values of Uc/SL. The arrow indicates increasing

values of Uc/SL. (b) Rescaled efficiency function as a

func-tion of a rescaled velocity ratio. The black dashed line rep-resent the fit using Eq. (4)

of Uθ/SL = 0.94, 1.43, 1.83 are presented in Fig. 7.

424

The increase of A(t,∆) is very nicely reproduced by

425

the simulation, whilst some slight departures are

ob-426

served close to the maximum of A(t,∆). This

indi-427

cates that the early stage of the interaction (i.e. before

428

the vortex reaches the burnt gas) relies mainly on a

429

kinematic interaction and that the heat release does

430

not play a significant role at this stage. The simulated

431

flame stretch compares favourably well with

experi-432

ments for the three cases represented in Fig. 7. A

433

scatter plot between the measured and simulated K0 max

434

for the entire database is further given in Fig. 8. Here

435

again, a nice agreement is observed. Departures

be-436

tween numerical and experimental data for K0 max lies

437

within 20% on average.

438

4.2. Formulation of a new efficiency function

439

By use of such numerical simulations, the effect of

440

Ucand Uθon Kmax0 can thus be studied independently

441

with the aim of incorporating these parameters in a

442

more complete expression for the efficiency function.

443

In Fig. 9(a), are provided the numerical results

444

for the efficiency function as a function of Uθ/SLfor

445

0.6SL≤ Uc− Uu(Xc) ≤ 4.7SL. Noticeable is the non

446

monotonic evolution of C with respect to Uθ/SLthat

447

was previously observed in the experiments (see Fig.

448

4). Furthermore, one clearly sees a dependence of C

449

on Uc. Note that for Uθ/SL > 3.5 the effect of Ucis

450

almost negligible. In Fig. 9(b), it is shown that the

451

evolution of C with respect to Ucand Uθcan collapse

452

on a single curve, when the rescaled efficiency

func-453

tion F = C × (U∗

c/SL)1/3is plotted as a function of

454

a rescaled velocity ratio U = (Uθ/SL) × (U∗c/Uθ)4/3,

455

where U∗

c = Uc− Uu(Xc)+ SL is the relative

ve-456

locity between the flame and the vortex centers [4].

457

This curve highlights a first zone for U < 2.5 where

458 0 100 200 300 400 0 100 200 300 400 0 100 200 300 400 0 100 200 300 400 0 100 200 300 400 100 200 300 400 K0 m a x[s− 1] meas ur ed C × Uθ / Rv # s − 1 $ 1 1.5 2 2.5 1 1.5 2 2.5 1 1.5 2 2.5 0 100 200 300 4000 100 200 300 400 1 1.5 2 2.5 (a) (c) (b) (d) Colin et al. Present Charlette et al. Bougrine et al. Uθ SL Uθ SL Uθ SL Uθ SL

Figure 10: Scatter plot of the experimental vs modelled flame stretch using the present efficiency function (a), that of Colin et al. [7] (b), Charlette et al. [8] (c) and Bougrine et al. [9] (d). Symbols are coloured by Uθ/SL

F scales as U1/3, and a second zone at larger U

459

for which F decreases as U−1/4. This trend can be

460

well fitted by the following parametric expression (the

461

black dashed line in Fig. 9(b))

462 F = U1/3      1+ U Umax !2      −7 24 , (4) from which C = F × (U∗ c/SL)−1/3can be recovered. 463

Umaxis the rescaled velocity ratio for which the

bend-464

ing of F is observed and was found to be equal to 2.5.

465

The ability of this expression for modelling the flame

466

stretch from the vortex strain is emphasized in Fig.

467

10. Departures between modelled and measured K0 max

468

are similar to Fig. 8, i.e. within 20%. The present

469

formulation for C further appears to be more adequate

470

than either that of Colin et al. [7], Charlette et al. [8]

471

or Bougrine et al. [9].

472

5. Conclusion

473

The present study is devoted to the exploration

474

of the flame stretch induced by a vortex dipole with

475

special emphasis on the strain-sweeping competition.

476

Both experiments and numerical simulations of a

stag-477

nation flame have been carried out, with the aim of

as-478

sessing the ability of available parametric expression

479

for describing the efficiency function. The outcomes

480

of the present study can be summarized as follows:

481

• It was first shown that, though based on the same

482

numerical data, C provided by both Colin et al.

483

[7], Charlette et al. [8] predict an increase of C

484

with respect to Uθ/SLwhereas that of Bougrine

485

et al. [9] emphasizes the opposite trend. In

addi-486

tion, all these expressions fail in describing the

487

non-monotonic evolution of C with respect to

488

Uθ/SLwhich is observed in both experimental

489

and numerical data.

(9)

• Secondly, by comparing experiments to

simpli-491

fied numerical simulations based on the

’isother-492

mal’ G-equation, it was shown that the early

493

stage of interaction is driven by a kinematic

in-494

teraction between the vortex and the flame. The

495

maximum flame stretch issued from such

nu-496

merical simulations is in agreement with

exper-497

iments.

498

• Finally, these simulations allow the effect of the

499

residence time of the vortex in the vicinity of the

500

flame to be investigated. A new parametric

ex-501

pression for the efficiency function is proposed

502

and compares favourably well with

experimen-503

tal data.

504

As mentioned in the introduction, strain and

sweep-505

ing effects are respectively representative of rather

506

small (ur) and large scales (u0) phenomena. This

in-507

dicates a priori that in a LES, C can be evaluated,

508

using the sub-grid scale velocity for Uθ and the

to-509

tal (resolved+ sub-grid scale) velocity for Uc. The

510

residence time also requires the knowledge of the

vor-511

tex sweeping direction compared to the flame normal

512

direction, for which a sub-model has yet been

devel-513

oped. Another important point concerns the fact that

514

in LES, the efficiency functions have to be integrated

515

over all the sub-grid scales. In previous studies, e.g.

516

[8], the integration was done in spectral space. It is

517

worth stressing that the integration over available

tur-518

bulent scales might not be necessary by keeping the

519

description in physical space (that of the structure or

520

correlation functions), in which the notion of

cumula-521

tive over turbulent scales is implicit (see e.g. [17]).

In-522

deed, in Ref. [17], use was made of an expression for

523

the turbulent strain (Eq. (1) in [17]) which represents

524

the strain due to the combined effect of all smaller

525

scales (as the structure function does, see e.g. [18]

526

p.11, or [19] p 366). This expression is thus

equiv-527

alent to the subgrid scale strain. Consequently, the

528

multiplication of the efficiency function by the latter

529

expression for the strain directly represents the flame

530

stretch of all smaller scales than the scale considered.

531

i.e. the subgrid flame stretch and there is no need for

532

spectral integration.

533

Further work will be devoted to exploring the

im-534

pact of the ratio R/δLon C by changing the diameter

535

of the vortex generator. We also plan to study in

de-536

tail the effect of fuel composition and especially the

537

Lewis number effects.

538

Acknowledgements

539

The financial support from the Agence National de

540

la Recherche under the project IDYLLE is gratefully

541

acknowledged. In this respect, we would like to thank

542

especially S. Richard, L. Selle and T. Poinsot for

fruit-543

ful discussions. We are also thankful to the CNRS,

544

the University of Orl´eans, and the French

Govern-545

ment Program ”Investissements d’avenir” through the

546

LABEX CAPRYSSES. FT acknowledges EADS for

547

its financial support. We also benefited from the

com-548

puting resources provided by CaSciModOT. We thank

549

Laurent Catherine for his technical assistance. We

550

are grateful to Seong Young Lee for providing us the

551

CHEMKIN PRO results.

552

References

553

[1] P.-H. Renard, D. Thevenin, J.-C. Rolon, S. Candel, 554

Prog. Energ. Combust. 26 (2000) 225–282. 555

[2] T. Poinsot, D. Veynante, S. Candel, J. Fluid Mech. 228 556

(1991) 561–606. 557

[3] W. L. Roberts, J. F. Driscoll, Combust. Flame 87 558

(1991) 245–256. 559

[4] M.-S. Wu, J. F. Driscoll, Combust. Flame 91 (1992) 560

310–322. 561

[5] W. L. Roberts, J. F. Driscoll, M. C. Drake, L. P. Goss, 562

Combust. Flame 94 (1993) 58–69. 563

[6] T.-W. Lee, D. Santavicca, Combust. Sci. Technol. 90 564

(1993) 211–229. 565

[7] O. Colin, F. Ducros, D. Veynante, T. Poinsot, Phys. 566

Fluids 12 (2000) 1843–1863. 567

[8] F. Charlette, C. Meneveau, D. Veynante, Combust. 568

Flame 131 (2002) 159–180. 569

[9] S. Bougrine, S. Richard, O. Colin, D. Veynante, Flow, 570

turbul. combust. 93 (2014) 259–281. 571

[10] J. F. Driscoll, Prog. Energ. Combust. 34 (2008) 91– 572

134. 573

[11] A. Kolmogorov, Proc. USSR Ac. of Sci. 30 (1941) 574

299–303. 575

[12] H. Tennekes, J. Fluid Mech. 67 (1975) 561–567. 576

[13] C. Poulain, N. Mazellier, L. Chevillard, Y. Gagne, 577

C. Baudet, Eur. Phys. J. B 53 (2006) 219–224. 578

[14] N. Bouvet, D. Davidenko, C. Chauveau, L. Pillier, 579

Y. Yoon, Combust. Flame 161 (2014) 438–452. 580

[15] W. Thielicke, E. J. Stamhuis, Journal of Open Research 581

Software 2 (2014) 30. 582

[16] R. Trieling, J. Van Wesenbeeck, G. Van Heijst, Phys. 583

Fluids 10 (1998) 144–159. 584

[17] F. Thiesset, G. Maurice, F. Halter, N. Mazellier, 585

C. Chauveau, I. G¨okalp, Combustion Theory and Mod-586

elling 20 (2016) 1–17. 587

[18] A. A. R. Townsend, The structure of turbulent shear 588

flow, Cambridge Univ Press, 1976. 589

[19] P. A. Davidson, Turbulence: an introduction for scien-590

tists and engineers, Oxford University Press, 2015. 591

Figure

Figure 2: Time sequence of Mie scattering images of a typ- typ-ical FVI (U θ /S L = 1.43)
Fig. 2. The vorticity field and flame contours are su-
Figure 4: E ffi ciency function C = K max 0 /(U θ /R v ) as a func- func-tion of U θ /S L
Figure 8: Maximum stretch K max 0 assessed by experiments versus K 0 max inferred from numerical simulations
+2

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