Ignition

  • Uploaded by: chikulenka
  • 0
  • 0
  • June 2020
  • PDF

This document was uploaded by user and they confirmed that they have the permission to share it. If you are author or own the copyright of this book, please report to us by using this DMCA report form. Report DMCA


Overview

Download & View Ignition as PDF for free.

More details

  • Words: 2,231
  • Pages: 17
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

AME 514 - Fall 2006 - Lecture 2

1

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

AME 514 - Fall 2006 - Lecture 2

2

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

AME 514 - Fall 2006 - Lecture 2

Still later

SL

DISTANCE

3

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

AME 514 - Fall 2006 - Lecture 2

4

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)

AME 514 - Fall 2006 - Lecture 2

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

AME 514 - Fall 2006 - Lecture 2

6

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)

AME 514 - Fall 2006 - Lecture 2

7

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 β1  α β ∞ R = e x p − 1 ; δ = ; S = e x p      z L  2 L e 2θ*  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

AME 514 - Fall 2006 - Lecture 2

8

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

AME 514 - Fall 2006 - Lecture 2

QuickTime™ and a Video decompressor are needed to see this picture.

9

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

β1  R e x p  −1  z= L e 2θ* 

δ

From computations by Tromans and Furzeland, 1986

AME 514 - Fall 2006 - Lecture 2

10

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

11

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−ε1− 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

12

Dynamic analysis  Joulin (1985)

Radius vs. time

Minimum ignition energy vs. ignition

duration AME 514 - Fall 2006 - Lecture 2

13

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

AME 514 - Fall 2006 - Lecture 2

14

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

AME 514 - Fall 2006 - Lecture 2

15

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?

10

1

0.1

ps laser ns laser Lewis & von Elbe Sloane & Ronney Ronney Kingdon & Weinberg

4

5

6

7

8

9

10

11

12

Mole percent CH4 in air Lim et al., 1996 AME 514 - Fall 2006 - Lecture 2

16

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.

AME 514 - Fall 2006 - Lecture 2

17

Related Documents

Ignition
June 2020 28
Ignition
June 2020 38
18 Ignition
November 2019 38
Ignition System
June 2020 16
Ignition System
May 2020 25
Ignition Test
April 2020 44

More Documents from "Mikko Esala"