Advanced fundamental topics Ignition
Basic concepts Mathematical theory Dynamics of ignition Effects of the state of the combustible mixture Effects of the characteristics of the ignition source Effects of the flow environment
More detailed information: http://ronney.usc.edu/Lecture2/AME514F06/AME514.ignition.review.pdf
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Basic concepts
Minimum ignition energy (mJ)
Experiments (Lewis & von Elbe, 1961) show that a minimum energy (Emin) (not just minimum T or volume) required to ignite a flame Emin lowest near stoichiometric (typ. 0.2 mJ) but minimum shifts to richer mixtures for higher HCs (why? Stay tuned…) Prediction of Emin relevant to energy conversion and fire safety applications
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Basic concepts
Unsuccessful ignition
Successful ignition Initial profile
Later Still later
TEMPERATURE
TEMPERATURE
Emin related to need to create flame kernel with dimension (δ ) large enough that chemical reaction (Ω ) can exceed conductive loss rate (α /δ 2), thus δ > (α /Ω )1/2 ~ α /(α Ω )1/2 ~ α /SL ~ δ Emin ~ energy contained in volume of gas with T ≈ Tad and radius ≈ δ ≈ 4α /SL T 4 π3 4 π3 (T ) 2k ∞ a d− ∞ ⇒ E ≈ δ ρ C T − T ≈ 0 . 3 δ ρ C T − T ≈ 3 4 α ) ) m in p(a d ∞ ∞ p(a d ∞ ∞ 3 3 3 S L
Initial profile Later
δ
DISTANCE
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Still later
SL
DISTANCE
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Predictions of simple Emin formula Since α ~ P-1, Emin ~ P-2 if SL is independent of P Emin ≈ 100,000 times larger in a He-diluted than SF6diluted mixture with same SL, same P (due to α and λ differences) Stoichiometric CH4-air @ 1 atm: predicted Emin ≈ 0.010 mJ ≈ 30x times lower than experiment (due to chemical kinetics, heat losses, shock losses …) … but need something more (Lewis number effects): 10% H2-air (SL ≈ 10 cm/sec): predicted Emin ≈ 0.3 mJ = 2.5 times higher than experiments Lean CH4-air (SL ≈ 5 cm/sec): Emin ≈ 5 mJ compared to ≈ 5000mJ for lean C3H8-air with same SL - but prediction is same for both
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Predictions of simple Emin formula
Minimum ignition energy (mJ)
Emin ~ δ 3ρ ∞ δ hard to measure, but quenching distance (δ q) (min. tube diameter through which flame can propagate) should be ~ δ since Pelim = SL,lim δ q/α ~ δ q/δ ≈ 40 ≈ constant, thus should have 2 Emin ~ δ q3P 10 Hydrogen (lean) Slope = 0.739 Correlation so-so Hydrogen (rich) 10
1
10
0
10
-1
10
-2
10
-3
Methane (lean) Methane (rich) Ethane (lean) Ethane (rich) Propane (lean) Propane (rich) Best fit to all data
Slope = 1
10
-6
10
-5
10
-4
10
-3
10
-2
Pressure * (quenching distance)
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10 3
-1
10 3
(atm cm )
5
0
More rigorous approach Assumptions: 1D spherical; ideal gases; adiabatic (except for ignition source Q(r,t)); 1 limiting reactant (e.g. very lean or rich); 1-step overall reaction; ρ D, λ , CP, etc. constant; low Mach #; no body forces Governing equations for mass, energy & species conservations (y = limiting reactant mass fraction; QR = its heating value)
∂ρ 1 ∂ 2 T = ρ T = c o n s t a n t +2 ( r ρv)=0 ρ ∞ ∞ ∂t r ∂r ∂ T 1∂ 2 k ∂ 2∂ T − E ρ C + ρ C r v T = r + ρ Q y Z e x p +Q (r,t) ( ) () p p 2 R 2 ℜ T ∂ t r∂ r r∂ r ∂ r ∂y 1∂ 2 ρ D∂ 2∂ y − E ρ +ρ v2 ( ry) = 2 r −ρ y Ze x p() ℜ T ∂t r∂ r r ∂ r ∂ r
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More rigorous approach Non-dimensionalize (note Tad = T∞ + Y∞QR/CP)
T Z e−β v E −β θ≡ ;τ≡tA e ;R≡r ;U≡ ; β ≡ T α∞ ℜ T α∞Z e−β a d a d T
y
k
Q (r,t)
ε≡ ∞;Y≡ ;L e≡ ;Ω ≡ T y∞ ρC ρ∞C Z e−β a d pD pT ∞ leads to, for mass, energy and species conservation
∂Y 1 ∂ 2 1θ1 ∂ 2∂ Y ∂(1/θ) 1 ∂ 21 + U R Y = R Y e x p − + 2 R U ( ) =0 2 2 ∂ ∂τ R∂R L e εR∂ R R ∂τ R ∂R θ ∂ θ 1 ∂ 2 θ1 ∂ 2∂ θ 1 +U 2 ( Rθ = 2 R +( 1 − ε) Y e x p −β( − 1 + Ω (R ,τ)θ ) θ ) ∂ ∂ τ R∂ R εR∂ R R
(( ))
( )
with boundary conditions
θ ( R , 0 ) = ε ; Y ( R , 0 ) = 1 ; U ( R , 0 ) = 0 f o r a l R
(Initial condition: T = T∞, y = y∞, U = 0 everywhere)
θ ( R , τ ) = ε ; Y ( R , τ ) = 1 ; U ( R , τ ) = 0 a s R → ∞ (At infinite radius, T = T , y = y , ∞
∂θ ∂Y ∂U = = =0a tR =0 a n d a s R ∂R ∂R ∂R
∞
U = 0 for all times)
→ ∞
(Symmetry condition at r = 0 for all times)
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1 − β − 1
θ
Steady (?!?) solutions If reaction is confined to a thin zone near r = RZ (large β ) 1−ε Rz R R >Rz : θ= +ε; Y=1− z R T* 1−ε * * L e R R < Rz : θ=θ* =constant ; Y=0
θ≡
T a d
=ε+
T T a d− ∞ o r T =T + ∞ L e L e
2 εL eα Z − δ β1 α β ∞ R = e x p − 1 ; δ = ; S = e x p z L 2 L e 2θ* SL β
This is a flame ball solution - note for Le < > 1, T* > < Tad; for Le = 1, T* = Tad and RZ = δ Generally unstable
R < RZ: shrinks and extinguishes R > RZ: expands and develops into steady flame RZ related to requirement for initiation of steady flame - expect Emin ~ Rz3
… but stable for a few carefully (or accidentally) chosen mixtures
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Steady (?!?) solutions How can a spherical flame not propagate??? 1.2 Temperature
T*
Fuel concentration T ~ 1/r
T Interior filled with combustion products
Reaction zone
Normalized temperature (T - T ) / (T - T ) f
C ~ 1-1/r
1 0.8 0.6
Propagating flame (δ/r = 1/10) f
0.4 0.2 0 0.1
Fuel & oxygen diffuse inward
Flame ball
1 10 Radius / Radius of flame
100
Heat & products diffuse outward
Space experiments show ~ 1 cm diameter flame balls possible Movie: 500 sec elapsed time
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QuickTime™ and a Video decompressor are needed to see this picture.
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Lewis number effects Energy requirement very strongly dependent on Lewis number!
1000 ε = 1/7 β = 10
R 3 / R 3(Le = 1) z z
100 10 1 0.1 0.01 0.001 0
0.5
1
1.5
2
Lewis number
F ro m th e re la tio n
β1 R e x p −1 z= L e 2θ*
δ
From computations by Tromans and Furzeland, 1986
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Lewis number effects
Ok, so why does min. MIE shift to richer mixtures for higher HCs? Leeffective = α effective /Deffective Deff = D of stoichiometrically limiting reactant, thus for lean mixtures Deff = Dfuel ; rich mixtures Deff = DO2 Lean mixtures - Leeffective = Lefuel Mostly air, so α eff ≈ α air ; also Deff = Dfuel CH4: DCH4 > α air since MCH4 < MN2&O2 thus LeCH4 < 1, thus Leeff < 1 Higher HCs: Dfuel < α air , thus Leeff > 1 - much higher MIE Rich mixtures - Leeffective = LeO2 CH4: α CH4 > α air since MCH4 < MN2&O2 , so adding excess CH4 INCREASES Leeff Higher HCs: α fuel < α air since Mfuel > MN2&O2 , so adding excess fuel DECREASES Leeff Actually adding excess fuel decreases both α and D, but decreases α more
C o n s t 1 C o n s t 2 C o n s t 3 αeff =αm ;D ~ + ix ~ O 2 M M M m ix m ix O 2 AME 514 - Fall 2006 - Lecture 2
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Dynamic analysis RZ is related (but not equal) to an ignition requirement Joulin (1985) analyzed unsteady equations for Le < 1
σ q( σ) dχ(s) d s χσ ( )ln(χσ ( ))+ =χσ ( )∫ 2 σ σ−s 0 d θ* 2 2 ( ) Θ R(σ) L e αt q≡ ;χ≡ ;σ≡4π 2 * 2 R 1 − ε R 1 − L e 4πλRzTad ( θ) z z
(χ , σ and q are the dimensionless radius, time and heat input) and found at the optimal ignition duration 2
1−ε1− L e 3 Em ≈ 1 4 β ρ C T − T R ( ) in a d p a d ∞ z ε θ*L e
which has the expected form Emin ~ {energy per unit volume} x {volume of minimal flame kernel} ~ {ρ adCp(Tad - T∞)} x {Rz3} AME 514 - Fall 2006 - Lecture 2
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Dynamic analysis Joulin (1985)
Radius vs. time
Minimum ignition energy vs. ignition
duration AME 514 - Fall 2006 - Lecture 2
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Effect of spark gap & duration Expect “optimal” ignition duration ~ ignition kernel time scale ~ RZ2/α Duration too long - energy wasted after kernel has formed and propagated away - Emin ~ t1 Duration too short - larger shock losses, larger heat losses to electrodes due to high T kernel Expect “optimal” ignition kernel size ~ kernel length scale ~ RZ Size too large - energy wasted in too large volume - Emin ~ R3 Size too small - larger heat losses to electrodes Sloane & Ronney, 1990
Kono et al., 1976
Detailed chemical model
1-step chemical model
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Effect of flow environment Mean flow or random flow (i.e. turbulence) (e.g. inside IC engine or gas turbine) increases stretch, thus Emin
Kono et al., 1984
DeSoete, 1984
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Effect of ignition source
Minimum ignition energy (mJ)
Laser ignition sources higher than sparks despite lower heat losses, less asymmetrical flame kernel - maybe due to higher shock losses with shorter duration laser source?
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0.1
ps laser ns laser Lewis & von Elbe Sloane & Ronney Ronney Kingdon & Weinberg
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Mole percent CH4 in air Lim et al., 1996 AME 514 - Fall 2006 - Lecture 2
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References De Soete, G. G.: 20th Symposium (International) on Combustion, Combustion Institute, 1984, p. 161. Dixon-Lewis, G., Shepard, I. G.: 15th Symposium (International) on Combustion, Combustion Institute, 1974, p. 1483. Frendi, A., Sibulkin, M.: "Dependence of Minimum Ignition Energy on Ignition Parameters," Combust. Sci. Tech. 73, 395-413, 1990. Joulin, G.: Combust. Sci. Tech. 43, 99 (1985). Kingdon, R. G., Weinberg, F. J.: 16th Symposium (International) on Combustion, Combustion Institute, 1976, p. 747.9924. Kono, M., Kumagai, S., Sakai, T.: 16th Symposium (International) on Combustion, Combustion Institute, 1976, p. 757. Kono, M., Hatori, K., Iinuma, K.: 20th Symposium (International) on Combustion, Combustion Institute, 1984, p. 133. Lewis, B., von Elbe, G.: Combustion, Flames, and Explosions of Gases, 3rd ed., Academic Press, 1987. Lim, E. H., McIlroy, A., Ronney, P. D., Syage, J. A., in: Transport Phenomena in Combustion (S. H. Chan, Ed.), Taylor and Francis, 1996, pp. 176-184. Ronney, P. D., Combust. Flame 62, 120 (1985). Sloane, T. M., Ronney, P. D., "A Comparison of Ignition Phenomena Modelled with Detailed and Simplified Kinetics," Combustion Science and Technology, Vol. 88, pp. 1-13 (1993). Tromans, P. S., Furzeland, R. M.: 21st Symposium (International) on Combustion, Combustion Institute, 1986, p. 1891.
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