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Burning Rate, Kinetic Coupling,and Mechanism Reduction
Yiguang Ju Mechanical and Aerospace Engineering
Princeton University
2007 AFOSR MURI Kick-Off MeetingGeneration of Comprehensive Surrogate Kinetic
Models andValidation Databases for Simulating Large
Molecular WeightHydrocarbon Fuels
Holiday Inn, Princeton100 Independence Way
Princeton, NJ 08540
September 17, 2007
Outline
•Identification of research problems
•Research targets
•Experimental and analytical methods
ParaffinsIso-paraffins Cycloparaffins Aromatics Naphthalenes
Fuel Component SelectionLimited understanding
DetailedModel B
DetailedModel C
DetailedModel D
DetailedModel A
Thermodynamic/Transport/Reaction -Rate Parameter Determination
Experimental Data• Ignition (RCM,ST)• Speciation (FR, ST)• Flames (HP/HT)
burning rateignitionextinctiondiffusion
• Soot characteristics (HPDC)
Minimization / Optimization / Validation
Greater understanding
Kinetic Coupling
Density Ignition criteriaViscosity C/H Ratio
Heat Release RateHeat Capacity
Flame TemperatureSooting Character
etc …
Surrogate Composition Formulation(emulation of physical/chemical properties)
JetFuels
SURROGATE FUEL
Validation
SingleComponents
Single Componentsand
Mixtures
Comparison
REDUCED MECHANISMSFor specificapplications
II
III
I
VI
V
IV
•Burning rate•Diffusion-Kinetic coupling•Mechanism reduction
Research Targets &
Where We Fitin The Roadmap
Problems: Burning Rates at High Pressures
ms.flow speed
lengtht
msSα
dflame speeyDiffusivitt
r
Lf
3100
30
11
102
3
22
===
====−
DME, Ф = 0.77, 10 atm Kobayashi et al. 10 atmQin & Ju, 2005
Yuan, Ju & Law, 2005
Relevant to ICE?
KaMSS
au
u −=10
Research Tasks
• Accurate measurements of flame speeds at elevated pressures by using spherical flames
• Understanding and modeling of transport-kinetic coupling
• Development of efficient reduced mechanism by considering transport-kinetic coupling
Experimental Methods: Flame Speed Measurements
• Challenges and methodologies to measure flame speeds at high pressures and temperatures accurately
Flame Speed Measurement: Spherical Flames1.
Constant volume method:
(High pressure & high temperature)without stretch correction but large pressure increase
Lewis (1934), Metghalchi (1980), Farrell (2004)…Assumption: Non-flame curvature (stretch) effect!
)3()()(
1)(3
/10
0
200
dtdP
PP
PPRRRS u
efu
γ
−=
)4()(11123/1
/10
000
0 −
⎥⎦
⎤⎢⎣
⎡−−
−⎟⎟⎠
⎞⎜⎜⎝
⎛+−≈
− γ
γγ PP
PPPP
PP
RL
SSS
e
eeu
u
uu
What if the stretch effect is not zero?Flame speed error will be:
Lu
: Markstein length from pressure history
Constant Volume Method:Stretch Corrected Flame Speed (SCFS) (H2 /air)
Chen et al. 2007
0.5
1
1.5
2
0 0.2 0.4 0.6 0.8 1Normalized flame radius, Rf /R0
Flam
e sp
eeds
nom
arliz
ed b
y S
L0 PREMIXwithout stretch correctionstretch corrected flame speed
1.0 1.01 1.02 1.05 1.1 1.2 1.5 2 3 4 5
Normalized pressure, P/P0
(Su0)
(Su)(SL)
Flame Speed Measurement: Spherical Flames:12.
Constant pressure method
(High pressure)
What if the burned gas velocity is not zero?Flame speed error will be:
with stretch correction & small pressure increase
Bradley (1972), Faeth (1992), Law (2000), Ju (2005), Peterson (2007)…
)1(/ ubfu VS ρρ=
)2(ˆˆ
f
b
u
uu
Vu
SSS
=−
≡ε
Assumption: Burned gas velocity is zero!
What causes non-zero burned gas velocity?Compression, non-symmetric flow, radiation…Q U
b
Constant Pressure Method: Compression Induced Burned Gas Velocity
Chen & Ju 2007
Q Ub
Nomalized spatial coordinate, r/R0
Nor
mal
ized
flow
velo
city
,a*U
/SL
0 0.25 0.5 0.75 1-0.6
-0.4
-0.2
0
0.2
0.4
0.6
0.8Velocity distribution V(r)
-30%
-20%
-10%
0%
10%
to Rf/R0
S u0 /S
L-1
from =0.1from =0.2from =0.3
0.2 0.3 0.4 0.5
use "Su=a*dRf/dt"neglect the compression effect
compression corrected flame speeduse "Su=a*(dRf/dt-Ub)"
Rf/R0
Rf/R0
Rf/R0
Constant Pressure Method:
Compression Corrected Flame Speed (CCFS)
Flame speed correction:
What If a Cylindrical Chamber is Used?
Princeton 8.3 cm 8.3 cm diadia. by 13 cm length,. by 13 cm length,10 cm dia. by 15 cm length,10 cm dia. by 15 cm length,
Outer Chamber
Inner Chamber
Mercury Lamp
Focus Lens
Collimating Lens
Decollimating Lens
Pinhole
High-Speed VideoCamera
Knife Edge
Permanentmagnet
Gas Releasing HolesQuartz Window
Tungsten Wire
Iron Plate
Pressure Sensor & GaugesOuter Chamber
Inner Chamber
Mercury Lamp
Focus Lens
Collimating Lens
Decollimating Lens
Pinhole
High-Speed VideoCamera
Knife Edge
Permanentmagnet
Gas Releasing HolesQuartz Window
Tungsten Wire
Iron Plate
Pressure Sensor & Gauges
Non-symmetrical flow induced burned gas velocity!
-5 -4 -3 -2 -1 0 1 2 3 4 5-5
-4
-3
-2
-1
0
1
2
3
4
5
Axial direction, z (cm)
Rad
ial d
irect
ion,
r (c
m)
What If a Cylindrical Chamber is Used?
High Pressure Flame Speed (Su
) MeasurementEffect of non-spherical flow, ub
≠0
?)1(*
=Δ⋅−=
−
f
f
u
uu
uu
sss σ
0
50
100
150
200
250
0 1000 2000 3000 4000Stretch (1/s)
Flame speed (cm/s)
0.5 cm
1.01.52.02.53.0
3.5
4.0
How to Improve Measurements: Potential Flow Model
Potential flow:
Ring source
Point source
{ } γγηγηπ
φπ
dzyx
tqr
tm⋅
+⋅−+⋅−+
⋅= ∫
2
02/1222 )]sin([)]cos([
)(4
)(
Prediction of Fame Speed Using Potential Flow
0
50
100
150
200
250
0 1000 2000 3000 4000Stretch (1/s)
Flame speed (cm/s)
Cylindrical Model (Rw=5 cm)
Cylindrical Experiment (Rw=5 cm)
Unconfined ModelUnconfined Model
Cylindrical Model
Rw = 5 cm
Cylindrical Experiment
Rw = 5 cm
Stretch (s-1)
Flam
e Sp
eed
(cm
-s-1
)
Flow-Corrected Flame Speed
M.P. Burke, Y. Ju, F.L. Dryer, Eastern States Meeting, Virginia 2007
150160170180190200210220230240250
0 500 1000 1500 2000 2500 3000 3500Stretch (1/s)
Cal
cula
ted
flam
e sp
eed
(cm
/s)
Uncorrected
Flow Corrected
⎟⎟⎠
⎞⎜⎜⎝
⎛−⋅= b
f
u
bu u
dtdr
sρρ
dtdr
s f
u
bu ⋅=
ρρ
wfw rrr 5.01.0 <<
H2
-air, Φ=3.0,1atm
X
Y
-1.5 -1 -0.5 0 0.5 1 1.5
-1.5
-1
-0.5
0
0.5
1
1.5
X
Y
-1 -0.5 0 0.5 1
-1
-0.5
0
0.5
1
Le=0.25 Le=2.0
•1D steady-state and transient simulation of counterflow flames
•2D direct simulation of transient spherical flame propagation
Modeling Approaches
How to Improve Measurements (Radiation Effects): One-Dimensional Direct Modeling
Temperature distribution Radiation heat loss distribution
Flame
Improving Measurements (Multi-Dimensional Effect):Adaptive Direct Modeling
X (mm)
Y(m
m)
-10 -5 0 5 10-10
-5
0
5
10
X (mm)
Y(m
m)
-10 -5 0 5-10
-5
0
5
10
Q3.75E+103.50E+103.25E+103.00E+102.75E+102.50E+102.25E+102.00E+101.75E+101.50E+101.25E+101.00E+107.51E+095.00E+092.50E+09
A
B
D
C
a. Adaptive unstructured grid b. Grids for spherical flames
c. Spherical flame propagation
Research Goal
• Measure the flame speeds and Markstein lengths of surrogate fuel components up to 30 atm in a wide range of equivalence ratios
2. Models for Transport-Kinetic Coupling
Transport-coupling regimes:• Diffusion of reactants modifies fuel flux
n-heptane, n-dodecane, oxygen…• Diffusion of intermediate species
modifies local C/H ratio, e.g. H2
,CH4
,C2
H4• Diffusion of radicals modifies kinetic
reaction rate (via H abstraction)e.g. H, O, …
Kinetic coupling between straight chain and aromatic molecules
Sensitivity of Transport Properties: Flame Temperature
0 20 40 60 80 100 120
-0.5
-0.4
-0.3
-0.2
-0.1
0.0
0.1
0.2
nC7H16 C6H5CH3
iC4H8
iC8H18
C3H6pC3H4
C2H6
C2H2C2H4
CH4
CO2
CO
O
H2O
H
Sen
sitiv
ity o
f fla
me
tem
pera
ture
on
diffu
sivi
ty
Species number
O2
Extinction of PRF + Toluene
Lewis Number, Le
Crit
ical
Igni
tion
Pow
er,Q
c
0.5 1 1.5 2 2.510-2
10-1
100
101
102
103
h=0.00h=0.01
(a)
Q ?
Lewis Number, Le
Crit
ical
Igni
tion
Pow
er,Q
c
0.5 1 1.5 2 2.510-2
10-1
100
101
102
103
h=0.00h=0.01
(a)
Q ?
Effect of Reactant Transport on Minimum Ignition Energy
Fuel molecular size
Experimental Measurements Using Steady StateCounterflow Flames
• Extinction limit & temperature• Species (reactants, intermediate species, and radicals (O, H, OH)
Understanding of transport-kinetic coupling
Numerical modeling
Modeling of Transport-Kinetic Coupling inTransient Mixing & Ignition Process
Tem
pera
ture
, spe
cies
, and
vel
ocity
0 L
T
YO
YF
V
0 L
T
YOYF
V
0 L
T
YO
YF
V
a.Homogeneous ignition b. Frozen diffusionignition
c. diffusion ignition
•Kinetic ignition delay•Transport-kinetic coupling (No mixing delay time)
Transport-kinetic coupling (with mixing delay time)
Mechanism Reduction
Current strategies• Reaction Rate Analysis (Peters et al.)• Graph relation analysis (Lu et al.)• Intrinsic Low Dimension Method (Mass & Pope)• Computational Singular Perturbation (Lam et al.)• High Dimensional Fitting
(Franklach et al.)
•Lead to similar size of reduced mechanism•Reduced mechanism remains large•Homogeneous system, diffusion flux is not included
Our Approach
Path analysis (including diffusion flux, forspecies & reaction reduction)
CSP time scale analysis (fast & slow species)
In-situ adaptive HDMR (fitting)
High Dimensional Modeling Representation: Piecewise Reusable Implementation of Solution
Mapping
))(( 11 nnr
nn t SySyy +Δ+= ++
nnHDMR
n ttf Syy Δ+Δ=+ ),(1
)x,...,x,x()x,(xf)(xf+ f = (x)f N21..12i
jijii
ii0HDMR Nj
f++∑∑≥
Explicit time marching: need to calculate minor species
HDMR fitting:
Time (s)
Tem
pera
ture
(K)
0.0E+00 2.0E-04 4.0E-04
1000
1500
2000
2500
HDMRODE
Example: Ignition of Methane-Air
Li, Chen, Ju, Rabitz et al., 2007
Conclusions• Accurate measurement of flame speeds at high
pressures by using a spherical bomb remains challenging. Physical processes such as flow compression, non-symmetrical flow motion, stretch, and radiation need to be included for accurate measurements.
• There are three different types of transport-kinetic couplings. New models to describe mixing and transport-kinetic coupling in non-premixed and transient ignition process are needed. Advanced computation methods and experimental data are needed to gain quantitative understanding of transport-
kinetic coupling.• New methodologies to generate computationally
efficient reduced mechanisms are needed. Adaptive HDMR and time splitting method are attractive approaches.