Title: Premixed flame propagation in Hele-Shaw cells: What Darrieus
1Premixed flame propagation in Hele-Shaw cells
What Darrieus Landau didnt tell you
- http//ronney.usc.edu/research
- Paul D. Ronney
- Dept. of Aerospace Mechanical Engineering
- University of Southern California
- Los Angeles, CA 90089-1453 USA
- National Tsing-Hua University
- October 7, 2005
2University of Southern California
- Established 125 years ago this week!
- jointly by a Catholic, a Protestant and a Jew -
USC has always been a multi-ethnic,
multi-cultural, coeducational university - Today 32,000 students, 3000 faculty
- 2 main campuses University Park and Health
Sciences - USC Trojans football team ranked 1 in USA last 2
years
3USC Viterbi School of Engineering
- Naming gift by Andrew Erma Viterbi
- Andrew Viterbi co-founder of Qualcomm,
co-inventor of CDMA - 1900 undergraduates, 3300 graduate students, 165
faculty, 30 degree options - 135 million external research funding
- Distance Education Network (DEN) 900 students in
28 M.S. degree programs 171 MS degrees awarded
in 2005 - More info http//viterbi.usc.edu
4Paul Ronney
- B.S. Mechanical Engineering, UC Berkeley
- M.S. Aeronautics, Caltech
- Ph.D. in Aeronautics Astronautics, MIT
- Postdocs NASA Glenn, Cleveland US Naval
Research Lab, Washington DC - Assistant Professor, Princeton University
- Associate/Full Professor, USC
- Research interests
- Microscale combustion and power generation
- (10/4, INER 10/5 NCKU)
- Microgravity combustion and fluid mechanics
(10/4, NCU) - Turbulent combustion (10/7, NTHU)
- Internal combustion engines
- Ignition, flammability, extinction limits of
flames (10/3, NCU) - Flame spread over solid fuel beds
- Biophysics and biofilms (10/6, NCKU)
5Paul Ronney
6Introduction
- Models of premixed turbulent combustion dont
agree with experiments nor each other!
7Introduction - continued...
- whereas in liquid flame experiments, ST/SL in
4 different flows is consistent with Yakhots
model with no adjustable parameters
8Motivation (continued)
- Why are gaseous flames harder to model compare
(successfully) to experiments? - One reason self-generated wrinkling due to flame
instabilities - Thermal expansion (Darrieus-Landau, DL)
- Rayleigh-Taylor (buoyancy-driven, RT)
- Viscous fingering (Saffman-Taylor, ST) in
Hele-Shaw cells when viscous fluid displaced by
less viscous fluid - Diffusive-thermal (DT) (Lewis number)
- Needed simple apparatus for systematic study of
DL, RT, ST DT instabilities their effects on
burning rates
9Hele-Shaw flow
- Flow between closely-spaced parallel plates
- Momentum eqn. reduces to linear 2-D equation
(Darcys law) - 1000's of references
- Practical application to combustion flame
propagation in cylinder crevice volumes
10Joulin-Sivashinsky (CST, 1994) model
- Linear stability analysis of flame propagation in
HS cells - Uses Euler-Darcy momentum eqn.
- Combined effects of DL, ST, RT heat loss (but
no DT effect - no damping at small l) - Dispersion relation effects of thermal expansion
(?), viscosity change across front (F) buoyancy
(G) on relationship between scaled wavelength (?)
and scaled growth rate (?) - Characteristic wavelength for ST
(?/6)(?uUw2/?av) smaller scales dominated by DL
(no characteristic wavelength)
11Objectives
- Measure
- Propagation rates
- Wrinkling characteristics
- of premixed flames in Hele-Shaw cells
- as a function of
- Mixture strength (thus SL) (but density ratio (?)
viscosity change (fb - fu) dont vary much over
experimentally accessible range of mixtures) - Cell thickness (w)
- Propagation direction (upward, downward,
horizontal) - Lewis number (vary fuel inert type)
- and compare to JS model predictions
12Apparatus
- Aluminum frame sandwiched between Lexan windows
- 40 cm x 60 cm x 1.27 or 0.635 or 0.32 cm test
section - CH4 C3H8 fuel, N2 CO2 diluent - affects Le,
Peclet - Upward, horizontal, downward orientation
- Spark ignition (3 locations, plane initiation)
- Exhaust open to ambient pressure at ignition end
- flame propagates towards closed end of cell
13Results - video - baseline case
- 6.8 CH4-air, horizontal, 12.7 mm cell
14Results - video - upward propagation
- 6.8 CH4-air, upward, 12.7 mm cell
15Results - video - downward propagation
16Results - video - high Lewis number
- 3.0 C3H8-air, horizontal, 12.7 mm cell (Le 1.7)
17Results - video - low Lewis number
- 8.6 CH4 - 32.0 O2 - 60.0 CO2, horizontal, 12.7
mm cell (Le 0.7)
18Results - stoichiometric, baseline thickness
19Results - stoichiometric, thinner cell
20Results - stoichiometric, very thin cell
21Broken flames at very low Pe, Le lt 1
- 6.0 CH4- air, downward, 6.3 mm cell (Pe 30(!))
22Results - qualitative
- Orientation effects
- Horizontal propagation - large wavelength wrinkle
fills cell - Upward propagation - more pronounced large
wrinkle - Downward propagation - globally flat front
(buoyancy suppresses large-scale wrinkles)
oscillatory modes, transverse waves - Thinner cell transition to single large tulip
finger - Consistent with Joulin-Sivashinsky predictions
- Large-scale wrinkling observed even at high Le
- Broken flames observed near limits for low Le but
only rarely not repeatable - For practical range of conditions, buoyancy
diffusive-thermal effects cannot prevent
wrinkling due to viscous fingering and/or thermal
expansion - Evidence of preferred wavelengths, but selection
mechanism unclear
23Lewis number effects
3.0 C3H8 - 97.0 air Horizontal propagation 12.7
mm cell, Pe 166
8.6 CH4 - 34.4 O2 - 57.0 CO2 Horizontal
propagation 12.7 mm cell, Pe 85
6.8 CH4 - 93.2 air Horizontal propagation 12.7
mm cell, Pe 100
24Results - propagation rates
- 3-stage propagation
- Thermal expansion - most rapid, propagation rate
(?u/?b)SL - Quasi-steady (slower but still gt SL)
- Near-end-wall - slowest - large-scale wrinkling
suppressed
25Results - quasi-steady propagation rates
- Horizontal, CH4-air (Le 1)
- Quasi-steady propagation rate (ST) always larger
than SL - typically ST 3SL even though u/SL
0! - Independent of Pe SLw/? ? independent of heat
loss - Slightly higher ST/SL for thinner cell despite
lower Pe (greater heat loss) (for reasons to be
discussed later)
26Results - quasi-steady propagation rates
- Horizontal, C3H8-air
- Very different trend from CH4-air - ST/SL depends
significantly on Pe cell thickness (why? see
next slide) - STILL slightly higher ST/SL for thinner cell
despite lower Pe (greater heat loss)
27Results - quasi-steady propagation rates
- C3H8-air (lean) Le 1.7, lower ST/SL
- C3H8-air (rich) Le 0.9, higher ST/SL ( 3),
independent of Pe, similar to CH4-air
28Results - quasi-steady propagation rates
- Horizontal, CH4-O2-CO2 (Le 0.7)
- Similar to CH4-air, no effect of Pe
- Slightly higher average ST/SL 3.5 vs. 3.0,
narrow cell again slightly higher
29Results - quasi-steady propagation rates
- Upward, CH4-air (Le 1)
- Higher ST/SL for thicker cell - more buoyancy
effect, increases large-scale wrinkling - no
effect of orientation for 1/8 cell - More prevalent at low Pe (low SL) - back to ST/SL
3 for high Pe
30Results - quasi-steady propagation rates
- Downward, CH4-air (Le 1)
- Higher ST/SL for thinner cell - less buoyancy
effect - almost no effect for 1/8 cell - More prevalent at low Pe (low SL) - back to ST/SL
3 for high Pe - How to correlate ST/SL for varying orientation,
SL, w ???
31Results - quasi-steady propagation rates
- Upward, CH4-O2-CO2 (Le 0.7)
- Higher ST/SL for thicker cell - more buoyancy
effect, increases large-scale wrinkling - less
effect of orientation for 1/8 cell - More prevalent at low Pe (low SL) - back to ST/SL
4 for high Pe
32Results - pressure characteristics
- Initial pressure rise after ignition
- Pressure constant during quasi-steady phase
- Pressure rise higher for faster flames
- Slow flame Fast flame
33Scaling analysis
- How to estimate driving force for flame
wrinkling? - Hypothesis use linear growth rate (?) of
Joulin-Sivashinsky analysis divided by wavenumber
(k) (i.e. phase velocity ?/k) scaled by SL as a
dimensionless growth rate - Analogous to a turbulence intensity)
- Use largest value of growth rate, corresponding
to longest half-wavelength mode that fits in
cell, i.e., k (2?/L)/2 - (L width of cell 39.7 cm)
- Small L, i.e. L lt ST length (?/6)(?uUw2/?av)
- DL dominates - ?/k constant
- Propagation rate should be independent of L
- Large L, i.e. L gt (?/6)(?uUw2/?av)
- ST dominates - ?/k increases with L
- Propagation rate should increase with L
- Baseline condition (6.8 CH4-air, SL 15.8
cm/s, w 12.7 mm) ST length 41 cm gt L -
little effect of ST
34Scaling analysis
- ST length smaller (thus more important) for
slower flames and smaller w - but these
conditions will cause flame quenching - how to
get smaller ST length without quenching? - ST length w (?/6)(?u/?av)(1/Pr)Pe for fixed
cell width, minimum Pe 40 set by quenching -
easier to get smaller ST length without quenching
in thinner cells
35(No Transcript)
36Effect of JS parameter
- Results correlate reasonably well with relation
- ST/SL 1 0.64 (?/kSL)
- - suggests dimensionless JS parameter IS the
driving force
37Effect of JS parameter
- Very similar for CH4-O2-CO2 mixtures
38Effect of JS parameter
- but propane far less impressive
39Image analysis - flame position
- Determine flame position
- Video frames digitized, scaled to 256 pixels in x
(spanwise) direction - Odd/even video half-frames separated
- For each pixel column, flame position in y
(propagation) direction (yf) is 1st moment of
intensity (I) w.r.t. position, i.e. - Contrast brightness adjusted to obtain good
flame trace
40Flame front lengths
- Front length / cell width - measure of wrinkling
of flame by instabilities - Relatively constant during test
- Higher/lower for upward/downward propagation
- Front length / cell width AT/AL lt ST/SL - front
length alone cannot account for observed flame
acceleration by wrinkling - Curvature in 3rd dimension must account for
wrinkling - Assume ST/SL (AT/AL)(U/SL), where U speed of
curved flame in channel, flat in x-y plane
41Flame front lengths
- Even for horizontally-propagating flames, AT/AL
not constant - decreases with increasing Pe - but
(inferred) U/SL increases to make (measured)
ST/SL constant!
42Flame front lengths
- AT/AL similar with propane - but (inferred) U/SL
lower at low Pe to make (measured) ST/SL lower!
43Flame front lengths
- AT/AL correlates reasonably well with JS growth
parameter for CH4-air and CH4-O2-CO2 - Less satisfying for C3H8-air (high Le)
- Expected trend - AT/AL increases as JS parameter
increases - but AT/AL gt 1 even when JS parameter lt 0
44Results - wrinkling characteristics
- Individual images show clearly defined wavelength
selection
45Results - wrinkling characteristics
- but averaging make them hard to see - 1/2 wave
mode dominates spectra
46Results - wrinkling characteristics
- Because relative amplitudes of modes evolve over
time -
47Results - wrinkling characteristics
- Shows up better in terms of amplitude x
wavenumber
48Wrinkling - different mixture strengths
- Modes 3 - 5 are very popular for a range of SL
49Wrinkling - different cell thicknesses
- Characteristic wavelength for ST 103 cm, 26 cm,
6.4 cm in 12.7, 6.35, 3.2 mm thick cells - for
thinner cells, ST dominates DL, more nearly
monochromatic behavior (ST has characteristic
wavelength, DL doesnt)
Run 108 9.5 CH4-air Horizontal propagation 6.35
mm cell
50Wrinkling - different orientations
- Upward more wrinkling at large scales (RT
encouraged) downward less wrinkling at large
scales smaller scales unaffected (RT dominant at
large wavelengths)
51Wrinkling - different fuel-O2-inerts, same SL
- Slightly broader spectrum of disturbances at low
Le, less at high Le
52Conclusions
- Flame propagation in quasi-2D Hele-Shaw cells
reveals effects of - Thermal expansion - always present
- Viscous fingering - narrow channels, high U
- Buoyancy - destabilizing/stabilizing at long
wavelengths for upward/downward propagation - Lewis number affects behavior at small
wavelengths but propagation rate large-scale
structure unaffected - Heat loss (Peclet number) little effect, except
U affects transition from DL to ST controlled
behavior
53Remark
- Most experiments conducted in open flames
(Bunsen, counterflow, ...) - gas expansion
relaxed in 3rd dimension - but most practical applications in confined
geometries, where unavoidable thermal expansion
(DL) viscous fingering (ST) instabilities cause
propagation rates 3 SL even when heat loss,
Lewis number buoyancy effects are negligible - DL ST effects may affect propagation rates
substantially even when strong turbulence is
present - generates wrinkling up to scale of
apparatus - (ST/SL)Total (ST/SL)Turbulence x
(ST/SL)ThermalExpansion ?
54Remark
- Computational studies suggest similar conclusions
- Early times, turbulence dominates
- Late times, thermal expansion dominates
- H. Boughanem and A. Trouve, 27th Symposium, p.
971.
55Future work
- Examine phase information, mode coupling
- Obstacles of specified wavenumber - examine
forced response - Linear growth behavior - need to suppress
instabilities until specified time / location
(e.g. acoustics, Clanet Searby PRL 1998) - Radial growth from point ignition (Sivashinsky
others)
56Thanks to
- National Tsing-Hua University
- Prof. C. A. Lin, Prof. T. M. Liou
- Combustion Institute (Bernard Lewis Lectureship)
- NASA (research support)